Patent Application
20080232038
This invention relates to the field of solid electrolyte capacitors. More specifically, this invention relates to an electrical field-enhanced method for conductive polymer impregnation into porous anodes in order to form the cathode in solid electrolyte capacitors.
Solid electrolytic capacitors, available with various forms of encapsulation, feature higher electrical capacitance in package sizes which are small when compared to other types of capacitors. Due to their high volumetric efficiency and reliability, miniature ‘chip’ solid electrolytic capacitors are especially suitable for surface mounting technology (SMT) applications and are increasingly being used in current microelectronics and communication applications.
A solid electrolytic capacitor consists of an anode, which is a high surface area, porous sintered pellet made from capacitor grade powders with an embedded or attached wire or foil conductor covered by a dielectric oxide layer, which is usually formed by anodizing the anode open-pore surface. The dielectric layer follows closely the contour of the open porosity in the sintered body. The anodized porous body, i.e. the capacitor anode, is then impregnated with a cathodic electrically conducting material, connected to a cathode lead wire or frame and then encapsulated in a suitable potting compound such as epoxy or other resin. The high open porosity surface area of the pellet is the dominant feature that allows the solid electrolytic capacitor to have better volumetric efficiency than any other type of capacitor. An example of a solid electrolytic capacitor 10 known in the art is shown in
Anodes of solid electrolyte capacitors made from the valve metals tantalum (Ta), niobium (Nb), aluminum (Al) and niobium oxide (NbO) dominate today's market.
Methods for forming capacitor anodes are well known in the art and include both mechanical pressing and electrophoretic deposition (EPD). Electrophoretic deposition processes are described in International Patent Applications WO 02/103728 and WO 2006/027767 both by the same applicant, the descriptions of which, including references cited therein, are incorporated herein by reference in their entirety.
In the prior art methods a cathode is formed on the free surface of the dielectric film by impregnation of a suitable cathode material, such as manganese dioxide (MnO2), or a conductive polymer. The cathode material should conform closely to the surface micro-topology of the convoluted oxide layer that is formed on the interconnected internal pore surface.
External connections for the capacitor cathode are made through thin conductive layers, typically formed from graphite and silver, applied by methods well known in the art.
Conductive polymers have an electrical conductivity that can be over 1000 times higher than the conductivity of MnO2, which is commonly used as the cathode material in conventional solid electrolyte capacitors. Therefore, cathodes made of conductive polymers are considered essential for low equivalent series resistance (ESR) solid electrolyte capacitors. There are two methods known in the art for impregnation of anodes with conductive polymers. Both are based on multi-step immersion in solution of monomer precursors and oxidizers for an in situ surface chemical polymerization process. Details can be found in: “PEDT as Conductive Polymer Cathode in Electrolytic Capacitors” Udo Merker, Ynud Reuter, Klaus Wussow, and Stephan Kirchmeyer, H. C. Starck GmbH and Ursula Tracht Bayer A G, presented to CARTS 2002. The monomer and oxidizer can be brought into the porous structure either sequentially or as a premixed solution. In the sequential process, the anode pellet is first dipped into an oxidizer solution, then the solvent is evaporated and the pellet is dipped into the monomer solution. After polymerization residual materials are washed out to open the pore structure for the next cycle. The major disadvantages of the sequential process are that for every cycle, two dips are necessary and the monomer and oxidizer cannot really be applied in a stoichiometric ratio.
For the premixed solution, process monomer and oxidizer are mixed in a solvent in a stoichiometric ratio. Then the anode pellet is dipped into the solution and dried. The advantages of this process are the use of stoichiometric mixtures and that only one dip is necessary for each cycle. Furthermore, conductive films made with premixed solutions have a much better quality and a higher conductivity than those made by sequential dipping. However, the thickness of conductive polymer layers that are achievable using current methods is limited to about twenty nanometers. This low cross-sectional area for electrical conduction increases the resistance of the cathode.
Examples of the use of polymers as electrically conducting solid cathodes are given in U.S. Pat. No. 6,519,137, U.S. Pat. No. 6,451,074, U.S. Pat. No. 6,391,379, and U.S. Pat. No. 6,361,572.
Although dispersions of conductive polymer particles in water or solvent are commercially available (for example, Baytron PH from H.C. Starck GmbH, a PEDT/PSS dispersion in water), the tendency to inhomogeneous, non-uniform and discontinuous surface coverage of the dielectric layer within the anode pores does not allow easy or effective impregnation of a porous anode pellet by simple dipping of the anode in such dispersions.
An example of commercially available materials for the preparation of premixed solutions is Baytron M (EDT), which is mixed with Baytron CE, both manufactured by H.C. Starck GmbH, Germany. Baytron M, consisting of 3,4-ethylenedioxythiophene (EDT; CAS number 126213-50-1), is a monomer for the production of PEDT conductive polymer coatings. Baytron CE is a 40% ethanolic solution of iron (III)p-toluolenesulfonate, an oxidizing agent based upon an iron(III) salt. One part by weight of Baytron. M is mixed with 20 parts of Baytron CE, providing a reactive mixture in a stoichiometric ratio of 2 mole iron (III) p-toluolenesulfonate per mole EDT. Three dips, dry and wash cycles are required to achieve full impregnation when using premixed solutions, where each cycle requires at least 30 minutes.
As already stated, cathodes of solid electrolytic capacitors like tantalum, niobium and niobium oxide are manufactured in accordance with the prior art by impregnation of the anode with a suitable material such as manganese dioxide (MnO2) or a conductive polymer. The method known in the art for impregnation of anodes with conductive polymers is immersion in monomer precursors for an in situ surface chemical polymerization process, where use of premixed solutions of the monomer and oxidizer is the generally preferred process.
Both the manganese dioxide process and the prior art conductive polymer process require multiple process cycles for implementation. Furthermore, the conductive polymer premix solutions result in waste due to short pot life. Also, the achieved conductive polymer coating from solution is very thin, only about 20 nm, limiting the potential reduction in capacitor ESR.
The limitations of conductive polymer could be overcome if it were possible to use fully polymerized conductive polymer as the cathode material instead of in-situ polymerization from monomer and oxidizer solutions. Although dispersions of conductive polymer particles in water or solvent are commercially available, lack of an efficient impregnation process does not allow impregnation of a porous tantalum anode pellet by dipping of the anode in such dispersions.
An object of the current invention is to provide a new and improved method to apply electrically conductive polymer films to the convoluted dielectric free surface of a solid electrolyte capacitor porous anode.
It is another objective of the current invention to provide a means to partially or fully impregnate highly conductive and viscous polymers into an open pore structure of sub-micron pores in the porous anode of a solid electrolyte capacitor.
Yet another objective of the current invention is to provide a method to apply a uniform polymer coating of controlled thickness on the external dielectric surface of solid electrolyte capacitor anodes.
Another objective of the current invention is to provide electric-field-enhanced methods to impregnate conductive polymer materials on convoluted dielectric surfaces.
Another objective of the current invention is to minimize the number of sequential steps required for impregnation of the cathode material and the time required for conducting each step.
Another objective of the current invention is to maximize utilization and minimize waste of the conducting polymer impregnation material.
Still another objective of the current invention it to provide an impregnation process that is suitable for use at room temperature.
Another objective of the current invention is to enhance control of the thickness, density, and uniformity of the conductive film applied as the cathode to the convoluted surface of the dielectric.
Another objective of the current invention is to preserve the mechanical, physical, chemical, and electrical properties of the dielectric layer on the convoluted internal surfaces of the open porosity of the anode and avoid any degradation of these properties.
Another objective of the current invention is to provide a solid electrolytic capacitor of any size having low ESR.
Yet another objective of the method of the invention is to provide for a high yield and low cost industrial process for the impregnation of a conducting polymer to form the cathode contact in the porous structure of an electrolytic capacitor.
Other objects and advantages of the invention will become apparent in the following description of this invention.
As opposed to the prior art methods, the method of the present invention uses electrophoretic deposition (EPD) to impregnate the anode with fully polymerized conductive polymer material from dispersions.
The invention described herein provides for a high yield and low cost industrial process with efficient materials utilization for the impregnation of conducting polymers to form the cathode contact in the porous structure of an electrolytic capacitor. The invention furthermore exploits high conductivity polymers and deposits these in relatively thick layers within the anode pores and onto the outer surface of the anode, allowing lower ESR capacitors to be produced.
In a first aspect the present invention is a method for forming a conductive polymer cathode for a solid electrolyte capacitor, the method comprising:
The voltage applied in the EPD cell can have a value that is slightly less than, equal to, or greater than the dielectric formation voltage. The voltage can be kept constant and the EPD current controlled at the power supply or the EPD cell current can be held constant. The constant EPD current can be in the range of 0.01 mA to 0.5 mA per mg of anode mass.
According to the method of the invention, the conductive polymer can coat the convoluted dielectric free surface of the pore structure within the solid electrolytic capacitor anode, the outer surface of the dielectric coated anode can be coated with conductive polymer during the EPD process of forming the cathode from the conductive polymer on the convoluted dielectric free surface of the pore structure within the solid electrolytic capacitor anode, and the EPD process can be used to coat with conductive polymer the outer surface of an anode previously impregnated with cathode material. The previously impregnated cathode material can be manganese dioxide, conductive polymer produced by in situ chemical polymerization, or conductive polymer deposited with EPD from a conductive polymer dispersion. Preferably the thickness of the external conductive polymer coating is at least 1 micrometer.
The conductive polymer can be any conductive polymer material that can be dispersed as particles in a liquid wherein the particles and the dispersion have characteristics that allow EPD to be performed. In preferred embodiments of the invention the conductive polymer material is chosen from the group comprising: polythiophene or derivatives thereof, polyaniline or derivatives thereof, and polypyrole or derivatives thereof.
The conductive polymer used to coat the convoluted dielectric free surface of the pore structure within the solid electrolytic capacitor anode should have a maximum electrical conductivity, at least higher than 30 S/cm. The conductive polymer used to coat the outer surface of an anode previously impregnated with cathode material should have a maximum electrical conductivity, at least higher than 50 S/cm.
The dispersion should have the following characteristics: concentration of the particles in the dispersion in the range of 1.5% to 10% by weight, viscosity in the range of 5 cP to 70 cP, Zeta potential lower than −30 mV, pH in the range of 1 to 3, and conductivity greater than 50 S/cm.
In order to coat the convoluted dielectric free surface of the pore structure within the solid electrolytic capacitor anode, the mean size of the particles in the dispersion should be smaller than the mean pore size within the anode. In order to coat with conductive polymer the outer surface of an anode previously impregnated with cathode material, the mean particle size in the dispersion should be smaller than 10 micrometers.
In another aspect, the invention is a solid electrolytic capacitor comprising a cathode made from a conductive polymer layer formed by an EPD process on the free surface of the dielectric coating of an anode body.
As is well known, EPD is carried out by applying a voltage between two electrodes immersed in a suitable dispersion. Persons familiar with the present state of the art would know that, if one of the electrodes is a substrate coated with a continuous dielectric layer, then current will not be able to flow between the electrodes and EPD deposition on the dielectric layer could not take place. In other words, EPD as it is presently applied cannot be used to form a conductive polymer layer within the open pore structure of a capacitor anode from a dispersion of the conductive polymer.
As opposed to the prior art methods of electrophoretic deposition, the present invention successfully deposits particles from dispersion on continuous, highly insulating dielectric layers. This invention enables electrophoretic deposition by use of EPD voltage near or above the anode dielectric formation voltage, where the anode body is positively biased relative to the EPD counter electrode. These high voltages allow a current to be driven through the dielectric layer. The conductive polymer dispersions are chosen such that the dispersed particles are negatively charged and therefore deposit within the pores and onto the outer surface of the positively biased anode.
This invention uses a positive bias on the anode body for EPD of the cathode material since a negative bias would electrochemically dissolve the dielectric layer. The high positive EPD bias that is used by the invention would also be expected to damage the dielectric, but this is prevented in the invention by limiting the deposition to times as short as 1 second or by the use of constant current power supplies that prevent catastrophic dielectric breakdown or both.
In the present invention, a constant EPD voltage having a value ranging from slightly below to higher than the dielectric formation voltage is applied for a short time, generating a current, which is limited at the power supply, through the anode dielectric. More preferably, the current is held to a constant value and the voltage is capped at a slightly lower, equal, or higher voltage than the dielectric formation voltage. It has been found that under these conditions conducting polymers meeting certain requirements, which will be detailed hereinbelow, can be uniformly deposited onto the dielectric surface throughout the anode pore structure.
The starting point of all embodiments of the invention is a porous solid electrolyte capacitor anode made by any prior art method including an EDP process as described in the above referenced international patent applications.
In a first preferred embodiment, The cathode is made by impregnating the anode with the conductive polymer. The preferred characteristics of the conductive polymer and of the EDP dispersion for the purpose of impregnating the anode, i.e., for penetrating the open pore structure of the capacitor anode to create a continuous conducting cathode on the dielectric surface of the open pore structure, are:
The conductive polymer has maximum electrical conductivity, at least higher than 30 S/cm.
The mean particle size of the conductive polymer in the dispersion is smaller than the mean pore size of the anode body.
The conductive polymer has thermal stability up to 260° C. for short exposure times, i.e., up to one minute, and thermal stability up to 175° C. for an exposure time of one hour.
In a second preferred embodiment, the electrophoretic impregnation process is used to produce an outer conductive polymer coating on the surface of the cathode impregnated anode, after which conductive carbon and silver coatings known in the art may be directly deposited onto said conductive polymer coating. The preferred characteristics of the conductive polymer and of the EDP dispersion for the purpose of coating the outer surface of the capacitor anode are:
For both of the preferred embodiments, the conductive polymer is selected from a group of materials that satisfies the above conditions and includes, for example, polythiophene and derivatives thereof, polyaniline and derivatives thereof and polypyroles, and derivatives thereof.
The group of suitable polythiophenes includes, for example, polyethylenedioxithiophene (PEDT), commercially available as Baytron PH, which comprises PEDT, an acid, and a matrix of polystyrene.
Conductive polymers from the group containing polythiophenes can be dispersed in liquids such as water and alcohols, e.g. ethanol. The concentration of said conductive polymer from said group of polythiopenes is preferably between 1.5% and 10% by weight.
The group of polypyrole derivatives can include polypyrole doped with acid. The conductive polymer from the group comprising polypyroles can be dispersed in a group of liquids including, for example, water, xylene, and alcohols, e.g. ethanol and isopropyl alcohol (IPA). The concentration of said conductive polymer from said group of polypyroles in the dispersion is preferably between 1.5% and 10% by weight.
A typical representative of the group of conductive polyaniline derivatives is polyaniline para-tolouene sulfonic acid (PTSA) commercially available dispersed at various concentrations in water from Ormecon (Germany) under the PANI brand name.
The conductive polymer from the group containing polyaniline can be dispersed in a group of liquids comprising, but not limited to, water, xylene, and alcohols, e.g. ethanol. The concentration of conductive polymer from the group of polyaniline in the dispersion is preferably between 1.5% and 10% by weight.
The characteristics of two of the formulations available from Ormecon, designated 6903-103-001 and and 6903-104-002 are listed in the following table.
In the first embodiment, i.e. impregnation of the open pore structure of the dielectric layer of the anode with conductive polymer, the temperature of the dispersion of conductive polymer during immersion is kept between SoC and 80° C. and the anode is immersed for a period of time ranging from 1 second to 30 minutes.
The process can be carried out at constant current in the range of 0.01 mA to 0.5 mA per mg anode mass, in which case the voltage will rise from slightly below or equal to the dielectric formation voltage to a limit which is set by the operator. The process can also be carried out at constant voltage as discussed hereinabove, in which case the current must be capped to prevent it from rising to the level that will destroy the dielectric coating. The electrophoretic impregnation process, if carried out long enough will simultaneously produce an outer conductive polymer coating on the surface of the anode, after which conductive carbon and silver coatings known in the art may be directly deposited onto the outer conductive polymer coating.
In the second embodiment referred to above a thick outer conductive polymer coating may be formed with any cathode material either polymer or inorganic by EPD on an anode previously impregnated by any of the methods known in the art or by EPD in accordance with the first embodiment of this invention.
In one embodiment of the coating process, the temperature of the emulsion of conductive polymer during immersion of the anode in the EDP cell is between 5° C. and 50° C. and the anode is immersed for a period of time ranging from 1 second to 30 minutes.
As in the case of impregnating the inner pore structure of the anode, the process can be carried out at constant current in the range of 0.01 mA to 0.5 mA per mg anode mass, in which case the voltage will rise from slightly below or equal to the dielectric formation voltage to a limit which is set by the operator. The process can also be carried out at constant voltage, in which case the current must be capped to prevent it from rising to the level that will destroy the dielectric coating.
As mentioned hereinabove, in different embodiments the outer conductive polymer coating can be applied using EPD onto an anode that was previously impregnated with conductive polymer cathode using EPD, that was previously impregnated with conductive polymer cathode using an in situ surface chemical polymerization process, or that was previously impregnated with manganese dioxide cathode using known dipping and pyrolysis processes. The preferred thickness of the outer conductive polymer coating formed by EPD is at least 1 micrometer.
External electrical connections for the cathode, which comprise a first conductive carbon layer and second silver layer, are applied after formation of the outer protective layer by methods well known in the art.
The following examples are provided merely to illustrate the invention and are not intended to limit the scope of the invention in any manner.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet that had been formed by electrophoretic deposition on a tantalum wire anode of 200 microns diameter and partially sintered in vacuum at 1200° C. The porous pellet was then immersed for 5 minutes in a solution of 100% Ormecon D1027 B50 PEDT dispersion, batch number 1027B50-00-50-050209-1 (manufactured by Ormecon GmbH, Germany). Mean Particle Size Distribution of this dispersion is 245 nm and conductivity is 54 S/cm. After dipping, the anode was dried in an oven at 100° C., washed in deionized water, and dried.
After the dipping and drying process, outer coatings of conductive carbon and silver were applied to the anode, providing electrical contact to the impregnated cathode for measurements. The outer coating process, which is well known in the art, was performed as follows:
1) Dip in Aquadag E carbon paste. The Aquadag E was diluted with deionized water before dipping: one part by weight Aquadag E to 4 parts DI water. The coating was allowed to dry for 30 minutes at room temperature. A standard cure was then performed in an oven by ramping at 5° C./minute to 100° C., holding for 30 minutes, and then cooling at 10° C./minute to room temperature.
2) Dip in 5262L polymeric Ag paste (manufactured by DuPont). The coating was allowed to dry for 20 minutes at room temperature. A standard cure was then performed in an oven by ramping at 5° C./minute to 80° C., holding for 15 minutes, further ramping at 5° C./minute to 175° C., holding for 60 minutes, and then cooling at 10° C./minute to room temperature.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surfaces of five NbO pellets that had been formed by electrophoretic deposition on a tantalum wire anode of 200 microns diameter and partially sintered in vacuum at 1200° C. The porous pellets were then immersed for 3 minutes in a solution of 100% Ormecon 6903-103-001 Lot 2 polyaniline (PANI) dispersion, manufactured by Ormecon GmbH, Germany. Mean Particle Size of this dispersion is 75 nm and conductivity is 60 S/cm. After dipping, the anodes were dried in an oven at 100° C., washed in deionized water and dried.
After the dipping and drying process, outer coatings of conductive carbon and silver were applied to the anodes using the same process described in Example 1, providing electrical contact to the impregnated cathode for measurements.
The measured capacitance of the five finished capacitors was 0.005 μF, 0.25 μF, 0.26 μF, 0.002 μF and 0.135 μF.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet made by electrophoretic deposition on a 200 microns diameter tantalum wire and partially sintered in vacuum at 1200° C. Dielectric formation voltage was 20V.
The pellet was then immersed in an EPD cell containing an Ormecon 6903-103-001 Lot 2 polyaniline (PANI) dispersion, manufactured by Ormecon GmbH, Germany. Mean Particle Size of this dispersion is 75 nm and conductivity is 60 S/cm. During immersion, an external voltage of 29 volts was applied for 2 seconds between the sintered pellet, the anode, and a cathode counter-electrode. Negatively charged PANI particles were deposited on the dielectric free surface of the convoluted, interconnected open pore structure.
The pellet prepared in Example 3 was then immersed for a further 5 seconds in an EPD cell containing a dispersion of Ormecon 6903-103-001 Lot 2. During the 5 seconds immersion time, an external voltage of 30 volts was applied between the sintered pellet, i.e. the anode, and a cathode counter-electrode. Negatively charged PANI particles were again deposited on the dielectric surface. The pellet was then dried.
Referring to
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet made by electrophoretic deposition on a 200 microns diameter tantalum wire and partially sintered in vacuum at 1200° C. Dielectric formation voltage was 20V.
The pellet was then immersed for 2 seconds in an EPD cell containing a 100% Ormecon D1027 B50 PEDT dispersion, batch number 1027B50-00-50-050209-1 (manufactured by Ormecon GmbH, Germany). Mean Particle Size of this dispersion is 245 nm and conductivity is 54 S/cm.
During the 2 seconds immersion time an external voltage of 29 volts was applied between the sintered pellet, the anode, and a cathode counter-electrode. Negatively charged PEDT particles were deposited on dielectric surfaces of the convoluted, interconnected open pore structure. The anode was then dried in an oven at 100° C., washed in deionized water and dried.
After EPD impregnation of the anode with conductive polymer, outer coatings of conductive carbon and silver were applied using the same process described in Example 1, providing electrical contact to the cathode for measurements.
Capacitance of the capacitor was then measured and found to be 1.03 μF.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet made by electrophoretic deposition on a 200 microns diameter tantalum wire and partially sintered in vacuum at 1200° C. Dielectric formation voltage was 20V.
The pellet was then immersed for 2 seconds in an EPD cell containing a 100% Ormecon 6903-104-002 Lot 1 PANI dispersion (manufactured by Ormecon GmbH, Germany). Mean Particle Size of this dispersion is 63 nm and conductivity is 167 S/cm.
During the 2 seconds immersion time an external voltage of 29 volts was applied between the sintered pellet, the anode, and a cathode counter-electrode. Negatively charged PANI particles were deposited on dielectric surfaces of the convoluted, interconnected open pore structure. The anode was then dried in an oven at 100° C., washed in deionized water and dried.
After EPD impregnation of the anode with conductive polymer, outer coatings of conductive carbon and silver were applied using the same process described in Example 1, providing electrical contact to the cathode for measurements.
Capacitance of the capacitor was then measured and found to be 0.82 μF. ESR was measured to be 2 ohms.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet made by electrophoretic deposition on a 200 microns diameter tantalum wire and partially sintered in vacuum at 1200° C. Dielectric formation voltage was 21V.
The pellet was then immersed for 1 minute in an EDP cell containing a 100% Ormecon 6903-103-001 Lot 2 PANI dispersion (manufactured by Ormecon GmbH, Germany). Mean Particle Size of this dispersion is 75 nm and conductivity is 60 S/cm.
During the 1 minute immersion time a constant current of 0.1 mA was applied to the sintered pellet, the anode, from a cathode counter-electrode. Voltage was limited to 21 volts in order not to exceed the original formation voltage. Negatively charged PANI particles were deposited on dielectric surfaces of the convoluted, interconnected open pore structure. The anode was then dried in an oven at 100° C., washed in deionized water and dried.
After EPD impregnation of the anode with conductive polymer, outer coatings of conductive carbon and silver were applied using the same process described in Example 1, providing electrical contact to the cathode for measurements.
Capacitance of the capacitor was then measured and found to be 1.7 μF. ESR was measured to be 3 ohms. Current leakage with an applied DC voltage of 6.8V was measured to be 0.04 μA.
A dielectric layer was formed by methods known in the art on the convoluted, open pore free surface of a NbO pellet made by electrophoretic deposition on a 200 microns diameter tantalum wire and partially sintered in vacuum at 1200° C. Dielectric formation voltage was 21V.
The pellet was then immersed for 1 minute in an EPD cell containing a 100% Ormecon 6903-104-002 Lot 1 PANI dispersion (manufactured by Ormecon GmbH, Germany). Mean Particle Size of this dispersion is 63 nm and conductivity is 167 S/cm.
During the 1 minute immersion time a constant current of 0.1 mA was applied to the sintered pellet, the anode, from a cathode counter-electrode. Voltage was limited to 21 volts in order not to exceed the original formation voltage. Negatively charged PANI particles were deposited on dielectric surfaces of the convoluted, interconnected open pore structure. The anode was then dried in an oven at 100° C., washed in deionized water and dried.
After EPD impregnation of the anode with conductive polymer, outer coatings of conductive carbon and silver were applied using the same process described in Example 1, providing electrical contact to the cathode for measurements.
Capacitance of the capacitor was then measured and found to be 1.2 μF. ESR was measured to be 4 ohms. Current leakage with an applied DC voltage of 6.8V was measured to be 0.06 μA.
Although embodiments of the invention have been described by way of illustration, it will be understood that the invention may be carried out with many variations, modifications, and adaptations, without departing from its spirit or exceeding the scope of the claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 170659 | Sep 2005 | IL | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/IL2006/001015 | 9/4/2005 | WO | 00 | 5/28/2008 |
