METHOD OF SELECTING ELECTROLYTES FOR HIGH CAPACITY ELECTRIC ENERGY ACCUMULATORS

Abstract: A method for selecting an electrolyte for a high capacity electric energy accumulator is described. An electrolyte to be tested is provided in the accumulator. A volt-ampere characteristic of the accumulator is measured and a disintegration voltage at which the electrolyte starts to disintegrate is determined. An electrolyte is selected which has the disintegration voltage higher than the working voltage range of the accumulator.

Description: Method of Selecting Electrolytes for High Capacity Electric Energy Accumulators This invention relates to a method of selecting electrolytes for high capacity electric energy accumulators. BACKGROUND OF THE INVENTION Prior art double layer electrolytic capacitors (KDC) consist of a pair of metal electrodes, one of which is covered by a dielectric film (for example, the anode film formed as a result of the chemical effect on the surface of the electrode) that does not allow the passage of electrolyte to the metal surface. A membrane (as a rule, it is of a fibrous structure), saturated with the electrolyte, is usually placed between the electrode. Such membrane functions as the electrolyte carrier. The electrodes-metal and metal covered with the dielectric film are inert in relation to the electrolyte provided that the conditions of their work are preserved (polarity, voltage). When a high capacity electric energy accumulator is used, such accumulator requires the development of a special method for choosing a suitable electrolyte. SUMMARY OF THE INVENTION The present invention provides a method for selecting electrolytes based on the distinctiveness of high capacity electric energy accumulators from other traditional electrolytic capacitors of double layer (KDC) in light of differences of conditions of its work. In accordance with an aspect of the present invention, there is provided a method for selecting an electrolyte for a high capacity electric energy accumulator. The accumulator having a working voltage range. The method comprises providing an electrolyte to be tested in the accumulator; measuring a volt-ampere characteristic of the accumulator; determining a disintegration voltage at which the electrolyte starts to disintegrate; and selecting an electrolyte which has the disintegration voltage higher than the working voltage range of the accumulator. In accordance with another aspect of the present invention, there is provided a method for selecting a working voltage range of a high capacity electric energy accumulator. The method comprising providing an electrolyte to be tested in the accumulator; measuring a volt-ampere characteristic of the accumulator; determining a disintegration voltage at which the electrolyte starts to disintegrate; and selecting a working range of the accumulator such that the working range does not exceed the disintegration voltage. Other aspects and features of the present invention will be readily apparent to those skilled in the art from a review of the following detailed description of preferred embodiments in conjunction with the accompanying drawings. BRIEF DESCRIPTION OF THE DRAWINGS The invention will be further understood from the following description with reference to the drawings in which: Figure 1 is a diagram showing a fragment of a charged electrolytic KDC; Figure 2 is a diagram showing a simplified model of a fragment of the charged EMONA elementary cell; Figure 3 is a diagram showing an enlarged part of the simplified model of Figure 2; and Figure 4 is graph showing a volt-ampere characteristic of EMONA. ' DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is suitably used for a high capacity electric energy accumulator, such as EMONA. The EMONA is a device, consisting of at least one, more often of several, cells, divided between themselves and from the current collectors by chemically inert conducting non-transparent for its electrolyte particle separators; each of such cells includes in itself a couple of electrodes consisting of one or several layers of chemically inert carbonised activated conducting fibrous material which has a developed surface, active centres and orderly structure; the electrode pair is divided within itself by a chemically inert non-conducting transparent for the electrolyte particles membrane. This device is enclosed in an air-tight body. The electrolyte that is used is a liquid substance (clear liquid, liquid mixture, solution, gel, etc.) in which the electrodes and the chemically inert non- conducting transparent for the electrolyte particles membrane are saturated. The electrolyte is usually found in the adsorbed form in the material of the electrodes and the membrane, while free volume of the electrolyte is absent. The electrolyte is in direct contact with the chemically inert conducting surface of both electrodes. Each cell of EMONA is originally symmetrical in relation to the chemically inert non-conducting transparent for the electrolyte particles membrane. The use in the EMONA of the above described construction of the cell and materials requires the development of a special method for choosing the electrolyte. Processes leading to the charging of the device (accumulation of the electric energy) and processes for its use in the electric chains (output of the stored energy) are substantially different from the processes taking place in the traditional chemical sources of current in electric KDC with the metallic electrodes, despite the fact that they do not go beyond the laws of saving the charge and energy. For comparison, fragments of charged capacitors are provided: that of the electric KDC with the metallic electrodes and that for EMONA. Figure 1 represents a fragment in which: 1 - the metallic electrodes (for example A1); 2 - the anode oxidizing layer - dielectric with the thickness d and dielectric constant E>2; 3 - porous membrane saturated with a dry electrolyte. Generally, the electrolyte is a highly viscous liquid containing polar molecules. When charging the capacitor, the applied electric field influences the polar molecules of the electrolyte so as to orientate their polarization as it is shown on Figure 1. In turn, the oriented molecules of the electrolyte cause the induced polarization of the molecules of the hard dielectric. As a result, the creation of the polarized charges of the dielectric in the electrolyte lead to the redistribution of the concentration in the metal "electron gas": on the anode - n.,, on the cathode - n 2 , provided that n 2 >n Therefore, the role of the electrolyte is limited to that of creating the polarized charges during the capacitor charging. The electro-capacity of the capacitor is defined only the thickness of the dielectric layer and its dielectric constant. The working voltage of the capacitor is in complete dependence from the qualities of the dielectric layer and the concentration of the conduction electrons, appearing in the inter-electrode space because of the "autoelectronic emission" of the electrons. According to the Fermi-Dirak statistics, such electrons always are present when the temperature is T>0K. When the capacitor is charged, additional favourable conditions are created which allow the increase in their concentration (when the value of d voltage of the electric field near the internal borders of metal can reach 10 4 -10 5 V/cm, therefore the electrolytic metal capacitors have large "leakage currents". When the voltage is increased, the dielectric breakdown takes place, at which time the electrolyte is decomposed and huge amounts of gas are emitted. These changes lead to the capacitor getting out of order. Such changes do not allow the use of such capacitors in the chain of alternating current, or at the polarity reversal. Therefore, one can use as the working voltage, voltage during which no breakdown of the dielectric layer takes place. When analysing the analogous fragment of the charged EMONA device, the available experimental results show absence of a certain polarity at the initial stage and the possibility of the polarity reversal after the charge; as a result of this, the possibility of using in the chain of alternate current. Furthermore, multiple experiments show that in the fibrous structures, under complicated conditions, many qualities of the liquids (broadcasting diffusion, viscosity, temperature of boiling and hardening, the coefficient of refraction and others) change considerably. The analysis of the structure of carbonised activated material by means of electronic microscopy, Auger spectroscopy, and others lead to the qualitative representation of its character: availability of two types of pores - micro-pores - size about (5-10)x10 ~10 m and macro-pores - size approximately 100x10 "10 m and more; distribution according to the size is impossible to define. At the same time, the process of carbonisation, according to the generally accepted view, and graphitization of the materials possible at the so called sp2- hybridization of the carbon valence electrons. In other words, the energetic state of the valence electrons is changed. Figure 2 represents a fragment of the charged EMONA in the simplified version (ideal variant), when at the time of charging a complete separation of positive and negative charges took place (for simplification, the charges are represented without the accompanying hydrate and solvate shells). Figure 3 shows an enlarged fragment. In Figures 2 and 3: 1 the current collectors (metal); 2 the inert conducting non-transparent for the electrolyte separators; 3 the electrodes made of the carbonised activated conducting fibrous material of orderly structure; and 4 the non conducing transparent for the electrolyte membrane. Since the "electronic gas" is absent in the carbon graphitized structures, such picture is possible only provided that the redistribution (deformation) of the electronic density of the surface or the transformation of the energetic condition of the carbon valence electrons. This phenomena reminds of the electronic polarization in the non-polar dielectrics. However, the graphitized carbon structures act as transmitting media and, therefore, it is possible to assume the availability of an "exchange" mechanism of their conductance. In any case, the changes in the electron density of the carbon surface must be compensated by the change in the concentration of the "electron gas" in the metallic current collectors, that is, similar to the metallic electrodes in the electrolytic KDC, they must contain both n., (similar to the anode) and n 2 (similar to the cathode), and n 2 >n 1 . This picture allows explanation of all phenomena observed during the use of a device in the chain of constant and alternative current. Therefore, in this situation the role of the electrolyte is different from that in the case of the electrolytic KDC. During the charge, a double electric layer is formatted immediately on the surface of the electrode, and it certain structuralization takes place. At the same time the structure that is deeper in its layer, simultaneously with the formation of the charge, creates a certain screening shield of the charges, located immediately at the surface of the material. From this picture it is possible to define the conditions necessary for the successful work of the capacitor. Since the redistribution of the charges takes place under the influence of the electric field, the maximum possible voltage will be such that it does not allow the charges' discharge at the surface of the material. When the voltage is higher than allowed, the charges at the surface will be discharged, and this will result in their neutralization. Since the charges closest to the surface start discharging first of all, once having discharged, they would decrease the area of the layer (partially screened shielded from further located charged layers). If one studying the characteristics of the capacitor at this stage, at these and higher levels of voltage, these characteristics would have to change. Our experience indicates that such changes do not reflect considerably on the capacity, yet the current of short circuit changes more drastically. It does not seem possible to define the voltage corresponding to the beginning of the electrolyte disintegration (the discharge of the charged particles at the surface of the electrode). For example, when the gas-forming carriers of the charge are discharged, the gas may be formed, or not, depending on the surface density of such charges in the layer closest to the porous carbon surface based on the above described. The above-noted reveals how the method of choosing the electrolyte and its working voltage for EMONA is defined. This method involves (a) taking measurements; (b) received data analysis; and (c) choosing the range of the working voltages. (a) Taking Measurements The volt-ampere characteristics of the elementary EMONA cells are measured with the electrolyte being tested on the short circuit current: l sc =f(U). Every time EMONA is charged to a certain voltage value U, (generally, starting from 0 volt with a certain step, provided that U | > U r 1. When the value of the charging coefficient is identical, for example, K ch =1.03, it represents the correlation between the voltage on EMONA at charging and the voltage remaining on EMONA after its disconnection from the charging device. The current of the short circuit is defined in the EMONA, charged this way and when disconnected from the charging device, for example with the help of the Oscillograph and the calibrated shunt. The volt-ampere characteristic received in this way looks similar for any kind of electrolyte, and is reflected on Figure 4 3 (curve O-e . Particularly, the characteristic received for 1 N water solution of the sulphuric acid revealed disintegration voltage of 1.6-1.7 volt, which coincides with the well-known for the disintegration voltage of such an electrolyte 1.67 volt. (b) Received Data Analysis From the analysis of the volt-ampere characteristic, one defines the point from which the angle of the curve starts to decrease, that is du dU changes its mark to the negative (.m on Figure 4). Voltage corresponding to the found point will indicate the voltage corresponding to the beginning of the electrolyte disintegration. At the same time dU dl is increasing. This can be called the internal resistance. With further increase in the internal resistance voltage, the short circuit current reaches its maximum and starts to decrease. Such increase and the internal resistance growth is irreversible. If one had to measure, after the discharge, this characteristic (curve O-e 2 ) at its initial point, it would correspond to the highest internal resistance of the previous cycle coincides with curve O-e.,. The polarity of the first and the following charge- discharge cycle does not influence the voltage corresponding at the beginning of the characteristic bending. (c) Choosing the Range of the Working Voltages The disintegration voltage found this way will represent the maximum possible voltage for such an electrolyte in the conditions of EMONA, U max . When EMONA is used, this electrolyte is fit to work at the level of charge voltage not higher than U max irrespective of the polarity. In order to increase the reliability of the electrolyte work within EMONA, the nominal working voltage U nom may be used, which is a voltage that is a little bit lower than the maximum voltage allowed. One would include the coefficient of supply K u (usually 1.2-1.4), that is U nom = U max /K u . Therefore, the working voltage U work for this electrolyte can be any voltage value of which does not exceed U nom (section of the characteristic 0- N on Figure 4). The working voltage selected this way must provide the guaranteed device power. During the work within the parameters of this range (a shaded part of Figure 4) one would provide stable parameters of EMONA and theoretically unlimited number of large discharge cycles, as well as the longevity of work, including, when plugging into the chain of pulsating or alternating current (one should remember that EMONA, as other traditional capacitors, is charged to the peak value of voltage). The selection of an electrolyte for an EMONA is based on the definition of the working capacity of a certain electrolyte in the conditions of EMONA on the basis of analysing the received volt-ampere characteristic. First, the volt-ampere characteristic of the EMONA sample is measured with the electrolyte being tested. The point on the characteristic is defined which corresponds to the voltage at the time of exceeding which becomes less than 0. Voltage corresponding to the point found above is considered the maximum allowed for such an electrolyte within the conditions of EMONA. The measurements of the volt-ampere characteristic are conducted on an elementary cell. They are conducted on the short circuit current. The characteristic is measured beginning with 0V, with a certain step, to the voltage where each following voltage is higher than the previous one. As a nominal voltage, voltage slightly less than that the maximum voltage is determined. The coefficient of storage is considered for the voltage K u = U max /U nom . The working voltage applied to one EMONA cell does not exceed the maximum voltage or the nominal voltage. The present invention as described above may define the allowed working regimes for any device which work according to the principles similar to those in EMONA. Also, the present invention may define the discharge voltage for any liquid substance (pure liquid, solution, melt, condensate, get, ash and their mixtures). While particular embodiments of the present invention have been shown and described, changes and modifications may be made to such embodiments without departing from the true scope of the invention.

Claims: What is claimed is: 1. A method for selecting an electrolyte for a high capacity electric energy accumulator, the accumulator having a working voltage range, the method comprising steps of: providing an electrolyte to be tested in the accumulator; measuring a volt-ampere characteristic of the accumulator; determining a disintegration voltage at which the electrolyte starts to disintegrate; and selecting an electrolyte which has the disintegration voltage higher than the working voltage range of the accumulator. 2. The method as claimed in claim 1 , wherein the determining step comprises a step of finding the disintegration voltage as a point of a curve defined by the volt-ampere characteristic at which the angle of the curve starts to decrease. 3. The method as claimed in claim 1 , wherein the step of providing an electrolyte comprises a step of providing one or more elementary cells, each having a pair of electrodes having a layer of chemically inert conducting layer, and the pair of the electrodes being separated by a chemically inert non- conductive membrane which is transparent for the electrolyte. 4. The method as claimed in claim 1 , wherein the measuring step comprises a step of conducting the measurement on an elementary cell of the accumulator. 5. The method as claimed in claim 1 , wherein the measuring step comprises a step of conducting the measurement on a short circuit current. 6. The method as claimed in claim 1 , wherein the measuring step comprises a step of conducting the measurement beginning with OV to a voltage where each following voltage is higher than the previous one. 7. The method as claimed in claim 6, wherein the conducting step comprises a step of incrementing the voltage at a predetermined step. 8. The method as claimed in claim 1 , wherein the determining step determines the disintegration voltage as a maximum voltage for the electrolyte in the accumulator. 9. The method as claimed in claim 8 further comprises a step of determining a nominal voltage based on the maximum voltage multiplied by a supply coefficient of the accumulator. 10. The method as claimed in claim 9, wherein the selecting step comprises a step of selecting an electrolyte which has the disintegration voltage higher than the nominal voltage range of the accumulator. 11. The method as claimed in claim 1 , wherein the accumulator is an EMONA. 12. The method as claimed in claim 1 , wherein the method further comprises a step of defining the discharge voltage for a liquid substance. 13. A method for selecting a working voltage range of a high capacity electric energy accumulator, the method comprising steps of: providing an electrolyte to be tested in the accumulator; measuring a volt-ampere characteristic of the accumulator; determining a disintegration voltage at which the electrolyte starts to disintegrate; and selecting a working range of the accumulator such that the working range does not exceed the disintegration voltage. 14. The method as claimed in claim 13, wherein the determining step comprises a step of finding the disintegration voltage as a point of a curve defined by the volt-ampere characteristic at which the angle of the curve starts to decrease. 15. The method as claimed in claim 13, wherein the step of providing an electrolyte comprises a step of providing one or more elementary cells, each having a pair of electrodes having a layer of chemically inert conducting layer, and the pair of the electrodes being separated by a chemically inert non- conductive membrane which is transparent for the electrolyte. 16. The method as claimed in claim 13, wherein the measuring step comprises a step of conducting the measurement on an elementary cell of the accumulator. 17. The method as claimed in claim 13, wherein the measuring step comprises a step of conducting the measurement on a short circuit current. 18. The method as claimed in claim 13, wherein the measuring step comprises a step of conducting the measurement beginning with OV to a voltage where each following voltage is higher than the previous one. 19. The method as claimed in claim 18, wherein the conducting step comprises a step of incrementing the voltage at a predetermined step. 20. The method as claimed in claim 13, wherein the determining step determines the disintegration voltage as a maximum voltage for the electrolyte in the accumulator. 21. The method as claimed in claim 20 further comprises a step of determining a nominal voltage based on the maximum voltage multiplied by a supply coefficient of the accumulator. 22. The method as claimed in claim 21 , wherein the selecting step comprises a step of selecting an electrolyte which has the disintegration voltage higher than the nominal voltage range of the accumulator. 23. The method as claimed in claim 13, wherein the accumulator is an EMONA. 24. The method as claimed in claim 13, wherein the method further comprises a step of defining the discharge voltage for a liquid substance.

Inventors: BORISENKO DMITRY N HM, BORISENKO NIKOLAY N DI, BORISENKO, DMITRY N. HM, BORISENKO, NIKOLAY N. DI
Applicants: BORISENKO DMITRY N HM, SELECT MOLECULAR TECHNOLOGIES, ZABOROVSKAYA SOPHIA HF, BORISENKO, DMITRY N. HM, SELECT MOLECULAR TECHNOLOGIES CORPORATION, ZABOROVSKAYA, SOPHIA HF
Application year: 2000
Main classification: G01R31
IPC codes: G01R31, H01G9, H01G13