AN ORGANIC ELECTROLYTE CELL

Abstract: An organic electrolyte cell comprises a negative electrode (2), a positive electrode (5) including a main active material composed of bismuth trioxide, the bismuth trioxide being heat treated, and an organic electrolyte comprising a salt dissolved in an organic solvent.

Description: This invention relates to organic electrolyte cells. In organic electrolyte cells having lithium as the negative electrode active material, various cells differing in operating voltage can be fabricated, but from the practical viewpoint these cells are roughly divided into a type having an operating voltage of about 3V and a type having an operating voltage of about 1.5V. As positive electrode active material for the 1.5V type, there are known cupric oxide, iron sulphide, iron disulphide, lead oxide and bismuth trioxide. A cell fabricated using bismuth trioxide has a high operating voltage of 1.5 to 1.8V and is especially advantageous for use where a large electric current discharge is necessary. The operating voltage of an organic electrolyte cell comprising lithium as the negative electrode active material and bismuth trioxide as the positive electrode active material is about 1.5V and since this type of cell is substantially equivalent in operating voltage to a conventional ordinary commercial cell using an aqueous alkali electrolyte, such as an alkali-manganese cell or a silver oxide cell, the organic electrolyte cell has an interexchangeability with such a conventional cell. Furthermore, since creep phenomenon observed in an alkali electrolyte is not caused in an organic electrolyte, leakage of the electrolyte is reduced, so that the self-discharge is small and the energy density is high. Because of these advantages, development of a cell having an excellent long-period reliability and a high energy density is expected. In the case where a cell of this type, for example, a button cell, is prepared, the positive electrode is formed in the following manner. Bismuth trioxide as the active material, an electrically conductive material, for example, a carbon powder such as graphite or carbon black or a metal powder and a resin binder such as a fluororesin or polystyrene are mixed at a predetermined ratio, and a predetermined amount of this positive electrode mixture is packed in a mould of a moulding machine and compression-moulded to obtain a pellet shaped positive electrode moulded body. The so-obtained positive electrode moulded body is heated and dried under reduced pressure at a temperature (up to about 300°C) not causing thermal decomposition of the resin binder or oxidation of the conductive material and, after the positive electrode has thus been dehydrated sufficiently, the positive electrode is assembled into a cell. Organic electrolyte cells comprising bismuth trioxide as the positive electrode active material are disclosed, for example in Japanese Laid-Open Patent Specification No. 12425/1977 and Japanese Patent Specification No. 49673/1984 which corresponds to U.S. Patent Specification No. 4,085,259. As the organic electrolyte of a cell of this type, there have been used solutions of ionisable salts such as LiClO₄, LiBF₄, LiPF₆ and LiSO₃CF₃ as the supporting electrolyte in aprotic organic solvents such as propylene carbonate (hereinafter referred to as "PC"), γ-butyrolactone, tetrahydrofuran, 1,2-dimethoxyethane (hereinafter referred to as "DME"), dioxolane and mixtures thereof. In general, the electrolyte of the cell should have various characteristics and in view of the cell performance the following properties are most important: (1) the ionic conductivity is high and the electrode reaction velocity is high; (2) the boiling point is high, the solidification point is low, and the range of the operating temperatures is broad; (3) the electrolyte is stable against the positive electrode and negative electrode materials and the like, and the solubilities of the positive electrode and the negative electrode materials are low; and (4) the decomposition voltage is high. An organic electrolyte formed by dissolving LiClO₄ in a mixed solvent of PC having a high boiling point, a low solidification point, a high dielectric constant and a high solubility of the supporting electrolyte and DME having a low viscosity is excellent in respect of the foregoing properties and therefore this organic electrolyte has frequently been used. As the electrically conductive material for the positive electrode of a cell of this type, there are known carbon powders such as graphite and acetylene black (carbon black which is called "cell black", prepared by thermal decomposition of acetylene) and metal powders. When discharge is carried out in a cell fabricated according to the abovementioned conventional process by using bismuth trioxide as the positive electrode material two discharge voltages are observed and a lower operating voltage is obtained at a discharge depth larger than 40%. Accordingly, when this cell is used for an instrument for which a large electric current discharge is necessary, a voltage necessary for normally operating the instrument cannot be obtained because of the lowered cell voltage even though a sufficient cell capacity is left. Especially in the case of such an instrument as an electronic watch or an electronic desk-top computer, an average consumption current is as small as several µ A and the life required for a cell is as long as several months to 10 years or longer. Also, a pulsating large current discharge is necessary for operating a lamp, a buzzer, a step motor or the like. A cell to be used for this purpose is required to have a long-period reliability and a large current discharge capacity. Therefore, the abovementioned problem is very serious. In order to solve such disadvantages, the present invention seeks to provide an organic electrolyte cell in which the capacity possessed by the cell can be effectively utilised to the end even in the case where the cell is continuously used over a long period with a large current pulsating discharge. Moreover, the present invention seeks to provide an organic electrolyte cell with an improved bismuth trioxide positive electrode so that the operating voltage of a cell of this type, especially the operating voltage at a discharge depth larger than 40%, is increased and the effective discharge capacity is improved. The present invention also seeks to provide an organic electrolyte cell in which the capacity possessed by the cell can be effectively utilised to the end. The present invention further seeks to provide an organic electrolyte cell where expansion of volume on discharge is reduced, whereby the reliability and stability of the cell in an instrument provided therewith are enhanced and simultaneously the discharge capacity per unit volume is increased. The present invention also seeks to provide an organic electrolyte cell with improved conductive material for the positive electrode so that the closed circuit voltage and the discharge capacity can be simultaneously increased without sacrifice to the discharge capacity of the cell overall. According to one aspect of the present invention, there is provided an organic electrolyte cell comprising a negative electrode, a positive electrode including a main active material composed of heat treated bismuth trioxide (Bi₂O₃), and an organic electrolyte comprising an organic solvent and a salt dissolved in the organic solvent, characterised in that the bismuth trioxide is heat-treated at a temperature above 800°C. Advantageously, the negative electrode comprises lithium as a negative active material, and the organic electrolyte comprises the organic solvent and a lithium salt or salts dissolved in the organic solvent. Preferably the bismuth trioxide is heat-treated at a temperature in the range of 800°C to 1000°C in air, an inert gas or vacuum. Advantageously, the bismuth trioxide is heat-treated at a temperature higher than its melting point. Preferably the bismuth trioxide is subjected to a quenching treatment after heat treatment. Preferably, the positive electrode includes an electrically conductive material. This, with advantage, may comprise conductive furnace black produced by the furnace type incomplete combustion method, or may comprise graphite and conductive furnace carbon black. It is preferred that the positive electrode contain less than 2% by weight of conductive furnace carbon black. The organic solvent may comprise a mixed solvent composed mainly of butylene carbonate and 1,2-dimethoxyethane. The organic solvent may further comprise ethylene carbonate. The amount of ethylene carbonate may be less than 50%. The preferred ratio of butylene carbonate to 1,2-dimethoxyethane is in the range 3/1 to 1/3, and is substantially 1/1. Preferably, the salt is comprised of lithium perchlorate, LiCℓO₄. The invention is illustrated, merely by way of example, in the accompanying drawings, in which:- Figure 1 is a diagram illustrating the relation between temperature for heat treatment of bismuth trioxide and discharge capacity; Figure 2 is a sectional view illustrating an embodiment of an organic electrolyte cell according to the present invention; Figure 3 is a diagram comparing cells prepared by using bismuth trioxide heat-treated at various temperatures with respect to discharge characteristics; Figure 4 is a diagram comparing discharge characteristics of cells under a constant resistance of 7.5 kΩ; Figure 5 is a diagram comparing change of discharge characteristics under storage at 80°C; Figure 6 is a diagram comparing cells with respect to change of pulsating discharge characteristics under storage at 80°C; and Figure 7 is a diagram comparing the discharge characteristics of cells under a constant resistance of 7.5 kΩ. The applicants have researched with a view to solving the abovementioned problems and, as a result, it has been found that if bismuth trioxide heat-treated at a temperature higher than 650°C is used as the positive electrode active material, the operating voltage of an organic electrolyte cell, especially the operating voltage at a discharge depth larger than about 40%, is increased and the effective discharge capacity is highly improved. More specifically, in preparing the positive electrode, bismuth trioxide is heated at a temperature higher than 650°C and the heat treated bismuth trioxide is then mixed with conductive material and a binder and is moulded into a predetermined shape. Any atmosphere not reducing bismuth trioxide can be used as the heat treatment atmosphere, and the heat treatment may be carried out in open air, in an inert gas or in a vacuum. When powdery bismuth trioxide is heat-treated at a temperature higher than 650°C, an aggregated body is formed by solidification during cooling because of sintering, melting or the like. Accordingly, in order to mix bismuth trioxide homogeneously with the conductive material or binder, it is preferred that the heat-treated bismuth trioxide is sufficiently pulverised into fine particles having a size smaller than 100 µm before the mixing. When bismuth trioxide is heat-treated at a temperature close to or higher than its melting point, that is, 820°C, molten bismuth trioxide is formed and a firm aggregate body is produced on cooling. Therefore, in this case, it is especially important that heat-treated bismuth trioxide should be sufficiently pulverised into fine particles. In the case where discharge is carried out in a cell fabricated by using bismuth trioxide heat-treated at a temperature higher than 650°C, the operating voltage, especially the operating voltage at greater than 40% discharge depth, is increased and therefore the effective discharge capacity to a certain cut-off voltage is highly improved. The reason why the operating voltage is improved according to the present invention has not been completely elucidated. However, it is presumed that the reason is probably as follows. If bismuth trioxide is heat-treated at a temperature higher than 650°C, atoms constituting respective particles of bismuth trioxide move violently and subtle changes are caused in crystal surfaces and inner structures of the respective particles, and the electrochemical activity is enhanced. In contrast, if the heat treatment temperature is lower than 650°C, this movement of atoms is small and therefore the operating voltage is not improved. The present invention will now be described in detail with reference to the following examples. EXAMPLE 1 A product obtained by heat-treating powdery bismuth trioxide having a purity of 99.99% at 300 to 1000°C for 5 hours, cooling the heat-treated product and pulverising it to a particle size smaller than 100 µm was used as positive electrode active material, and an untreated powdery bismuth trioxide was used as comparative positive electrode active material. The heat-treated and untreated bismuth trioxide were each mixed with a carbonaceous conductive material (graphite or carbon black) and a binder composed of a fluororesin at a mixing weight ratio of 94.5/5/0.5. The mixture was compression-moulded into a pellet together with a positive electrode holding ring of stainless steel having an L-shaped section, and the moulded pellet was heated and dried at 100°C for 10 hours under reduced pressure to form a positive electrode having a diameter of 9.0 mm, a thickness of 1.1 mm and a theoretical capacity of 90 mAh. Figure 2 is a sectional view of one embodiment of an organic electrolyte cell according to the present invention. A negative electrode container 1 acts also as a negative electrode terminal. The negative electrode container 1 is obtained by draw-forming a nickel/stainless steel clad sheet having a thickness of 0.22 mm. A negative electrode 2 is formed by punching a lithium sheet having a thickness of 1.3 mm into a disk having a diameter of 6.4 mm and then press-bonding the disk to the inner surface of the negative electrode container 1. A positive electrode container 6 acts also as a positive electrode terminal, and is obtained by draw-forming a nickel/stainless steel clad sheet having a thickness of 0.22 mm. A positive electrode 5 is packed into the positive electrode container 6 and a separator 4, composed of a microporous polypropylene sheet, is placed on the positive electrode. An impregnating member 3 holds an electrolyte between the positive electrode and the negative electrode, and is formed of a non-woven fabric composed mainly of polypropylene. A gasket 7 composed mainly of polypropylene is interposed between the negative electrode container 1 and the positive electrode container 6 to keep electric insulation between the positive electrode and the negative electrode. The cell is sealed to prevent leakage by inwardly bending the opening edge of the positive electrode container and caulking the same. A solution of 1 mole/l of lithium perchlorate in a 1/1 mixed solvent of propylene carbonate and 1,2-dimethoxyethane is used as the electrolyte. The size of the cell is such that the outer diameter is 9.5 mm and the total thickness is 3.0 mm. Figure 3 shows the discharge characteristics of the cell shown in Figure 2 at 24°C under a constant resistance of 3 kΩ, in which curve a shows the result obtained when the bismuth trioxide was not heated, curve b shows the result obtained when the heat treatment temperature was 500°C, curve c shows the result obtained when the heat treatment temperature was 650°C, curve d shows the result obtained when the heat treatment temperature was 800°C and curve e shows the result obtained when the heat treatment temperature was 1000°C. From these results, it can be seen that if the temperature of the heat treatment of the bismuth trioxide is higher than 650°C, the discharge voltage, especially the discharge voltage in the latter half flat voltage portion of a larger than about 40% discharge depth, is increased and the discharge time to the cut-off voltage of 1.2V is prolonged. Thus, it will be appreciated that the discharge characteristics and the effective discharge capacity are prominently improved. Figure 1 illustrates the relation between the temperature for the heat treatment of bismuth trioxide and the discharge capacity. It is seen from Figure 1, that if the temperature for the heat treatment of bismuth trioxide is higher than 65°C, the discharge capacity is abruptly increased at heat treatment temperatures of about 800°C, increase of the discharge capacity is saturated at heat treatment temperatures higher than 850°C and if the heat treatment temperature is further elevated, the discharge capacity is hardly increased but is substantially constant. It is construed that the reason is that since the melting point of bismuth trioxide is 820°C and bismuth trioxide is in the stable molten state at temperatures higher than 820°C, even if bismuth trioxide is heated to temperatures higher than 820°C, the state after cooling is substantially the same. If the heat treatment temperature is higher than 850°C, there is very little further increase of capacity. In view of this fact, the cost of a heat treatment apparatus such as an electric furnace, the running cost of the heat treatment apparatus and the handling difficulty of bismuth trioxide, it is preferred that the heat treatment be carried out at up to 1000°C. EXAMPLE 2 An organic electrolyte cell was prepared in the same manner as described in Example 1, except that the heat treatment of bismuth trioxide was carried out in nitrogen gas. The cell was discharged under a constant resistance of 3 kΩ at 24°C in the same manner as described in Example 1. The obtained results were substantially the same as those obtained in Example 1. EXAMPLE 3 An organic electrolyte cell was prepared in the same manner as described in Example 1 except that the heat treatment of bismuth trioxide was carried out under reduced pressure of 1.3332236 Pa to 1.3332236 Pa (10⁻² to 10⁻³ Torr). The cell was discharged under a constant resistance of 3 kΩ at 24°C in the same manner as described in Example 1. The obtained results were substantially the same as those obtained in Example 1. Organic electrolytes formed by dissolving ionisable salts such as LiClO₄, LiBF₄, LiPF₆ and LiCF₃SO₃ as the supporting salt in aprotic organic solvents such as γ-butyrolactone, propylene carbonate, butylene carbonate, 1,2-dimethoxyethane, tetrahydrofuran, dioxolane, dimethylformamide and mixtures thereof can be used as the organic electrolyte. Preferably the bismuth trioxide is obtained by melting and heat-treating bismuth trioxide at a temperature higher than the melting point (about 820°C) and rapidly cooling the melt to solidify it. According to such treatment, not only the discharge characteristic but also the storage characteristic can be highly improved. An atmosphere not reducing bismuth trioxide to metallic bismuth or BiO can be used for melting bismuth trioxide and rapidly cooling the melt. Namely, the melting and rapid cooling treatments can be carried out in open air, in an inert gas or under vacuum. Any process can be adopted for melting and rapidly cooling the bismuth trioxide because deterioration by oxidation or reduction of bismuth trioxide or reaction with other substances is not caused and solidification is completed in a short time. For example, there may be adopted a process in which bismuth trioxide heated and melted in an electric furnace or the like is cast in a vessel of an anti-corrosive metal such as stainless steel (for example, SUS304 by Japanese Industrial Standard (JIS)) or platinum or a ceramic material such as alumina, maintained at a temperature lower than the melting point of bismuth trioxide, preferably a temperature lower than normal (room) temperature. Furthermore, in the case where bismuth trioxide subjected to the melting and rapid cooling treatments is used as the positive electrode, in order to mix bismuth trioxide uniformly with a carbonaceous conductive agent and/or a binder as required, it is preferred that the cooled and solidified mass of bismuth trioxide be pulverised into fine particles having a size smaller than about 100 µm. In the organic electrolyte cell having bismuth trioxide subjected to the melting and rapid cooling treatments as the positive electrode active material, the discharge characteristic and storage characteristic are highly improved over those of a cell having bismuth trioxide not heat-treated. The reason why the discharge characteristic is improved by the heat treatment of the bismuth trioxide and the storage characteristic is improved by the rapid cooling treatment after melting has not been completely elucidated, but it is presumed that the reason is probably as described below. Namely, bismuth trioxide includes various crystal forms, such as the α-form of the monoclinic system, the β-form of the tetragonal system obtained by transition at 700 to 710°C and the γ-form of the cubic system. Ordinarily, the α-form is readily formed if bismuth trioxide is melted and solidified by gradual cooling, and the γ-form is readily formed by rapid cooling. A great difference of the crystal state is brought about by the difference of the cooling method and it is estimated that also the surface condition of particles is greatly changed according to the cooling method. It is presumed that this difference will probably result in a difference of the stability of the cell with the lapse of time when bismuth trioxide is used as the positive electrode active material for an organic electrolyte cell. EXAMPLE 4 A button type cell was constructed using the same components as shown in Figure 2. The negative electrode container acts also as a negative electrode terminal, which is obtained by drawing a nickel/stainless steel/nickel three-layer clad sheet. The negative electrode is formed by punching a lithium sheet having a thickness of 1.4 mm into a disk having a diameter of 6.2 mm, the disk being press-bonded to the inner surface of the negative electrode container. The positive electrode container is formed of nickel-plated stainless steel, which also acts as a positive electrode terminal. The positive electrode, as described below, is packed in this positive electrode container, and a separator composed of a microporous polypropylene film is placed thereon. The gasket is composed mainly of polypropylene, which is interposed between the negative electrode container and the positive electrode container to keep electric insulation between the positive electrode and negative electrode, and by bending inwardly the opening edge of the positive electrode container and caulking it, the contents in the cell are sealed. In the present example, a solution obtained by dissolving lithium perchlorate at a concentration of 1 mole/l in a 45/5/50 mixed solvent of butylene carbonate, ethylene carbonate and 1,2-dimethoxyethane. The size of the cell was such that the outer diameter was 9.5 mm and the total thickness 3.0 mm. Three positive electrodes were prepared according to the following procedures. Commercially available bismuth trioxide powder having a purity of 99% was melted and heat-treated at 900°C for 5 hours in an electric furnace, and the molten bismuth trioxide was cast in a vessel of stainless steel (SUS304) placed on a heat-discharging iron plate maintained at normal temperature (about 20°C) to rapidly cool the melt and solidify it into a flat sheet having a thickness of about 1 mm. The time required for completely solidifying the melt of bismuth trioxide was several seconds at the most. The solid cooled almost to normal (room) temperature was pulverised to a particle size smaller than 100 µm. A positive electrode active material (a) composed of bismuth trioxide powder subjected to the abovementioned melting and rapid cooling treatments was obtained. Commercially available bismuth trioxide powder was similarly melted and heat-treated at 900°C for 5 hours in an electric furnace, and the switch of the electric furnace was turned off and the melt was naturally cooled for almost a day and a night in the electric furnace. The cooled solid was pulverised to a size smaller than 100 µm and obtained was a positive electrode active material (b). The so-obtained positive electrode active material (a) or (b) composed of bismuth trioxide powder or a positive electrode active material (c) composed of untreated commercially available bismuth trioxide powder as a comparison, was mixed with a carbonaceous conductive agent (graphite or carbon black) and a binder composed of polytetrafluoroethylene at a weight ratio of 94.5/5/0.5, and the mixture was compression-moulded into a pellet together with a positive electrode-holding ring having an L-shaped section and the pellet was heated and dried at 100°C under sufficiently reduced pressure to obtain a positive electrode. Each positive electrode had a diameter of 9.0 mm and the weight of the electrode mixture was 0.28 g. By using the so-obtained three positive electrodes, three cells which were the same except for the positive electrode were prepared. Discharge characteristics of these three cells under a constant resistance of 7.5 kΩ at 20°C are shown in Figure 4. The relation between the discharge capacity and the storage period, observed when these cells were stored for a predetermined period at 80°C, the discharge being similarly carried out under a constant resistance of 7.5 kΩ at 20°C, is shown in Figure 5. The cut-off voltage level was 1.2V. The lowest voltage obtained when the cells were stored in an atmosphere maintained at 80°C for a predetermined period as in Figure 5 and pulsating discharge of 7.8 mS was carried out at -10°C and 2 Kohm is shown in Figure 6. As seen from Figure 4, when the cells (a) and (b) having bismuth trioxide subjected to the melting heat treatment as the positive electrode active material are compared with the cell (c) having untreated bismuth trioxide as the positive electrode active material, in the former cells the discharge voltage in the latter half flat voltage portion of more than about 40% discharge depth is higher and the time of the discharge to the cut-off voltage of 1.2V is longer, and the former cells are highly improved in discharge characteristics and effective discharge capacity. It is also found that there is no substantial difference in the discharge characteristics between the cell (a) having bismuth trioxide subjected to the rapid cooling treatment after the melting heat treatment and the cell (b) having bismuth trioxide gradually cooled after the melting heat treatment. From Figures 5 and 6, it is seen that the cell (a) having bismuth trioxide subjected to the melting heat treatment and rapid cooling treatment is highly improved over the conventional cell (c) having untreated bismuth trioxide in its discharge capacity and pulsating discharge voltage after long-period storage at a high temperature (80°C), but the cell (b) having bismuth trioxide gradually cooled after the melting heat treatment is not improved but rather degraded in these characteristics. Namely, it is seen that the storage characteristic is greatly influenced by the cooling method after the heat treatment, and the rapid cooling is very effective. EXAMPLE 5 In this Example, a product obtained by melting and heat-treating bismuth trioxide at 1100°C in an argon atmosphere, rapidly cooling the melt in the argon atmosphere, pulverising the solid to a size smaller than 100 µm and classifying the particles was used as a positive electrode active material. A solution obtained by dissolving lithium perchlorate at a concentration of 1 mole/l in a 1/1 mixed solvent of propylene carbonate and 1,2-dimethoxyethane was used as the organic electrolyte. A cell was prepared in the same manner as in Example 4 except for these changes. When the cell was subjected to a storage test under a constant resistance of 7.5 Kohm and at a temperature of 80°C in the same manner as described in Example 4, it was found that the storage characteristic was substantially at the same level as that of the cell (a) obtained in Example 4. EXAMPLE 6 A cell was prepared in the same manner as described in Example 4 except the bismuth trioxide was melted and heated at 850°C under a reduced pressure of 1.3332236 Pa to 0.13332236 Pa (10⁻² to 10⁻³ Torr) and then the melt was rapidly cooled. When the so-obtained cell was subjected to a storage test under a constant resistance of 7.5 kΩ and at a temperature of 80°C in the same manner as described in Example 4, it was found that the storage characteristics of the cell was substantially at the same level as that of the cell (a) obtained in Example 4. In this Example, the melting heat treatment temperatures were only 850°C, 900°C and 1100°C, but the gist of the present invention resides in that the melting heat treatment of bismuth trioxide is carried out at a temperature higher than the melting point of bismuth trioxide and the melt is rapidly cooled and solidified (coagulated) and it is sufficient if the treatment is carried out within a temperature range (or an atmosphere) where the composition of bismuth trioxide is not substantially changed by reduction, thermal decomposition or the like. In general, bismuth trioxide is very stable against heating at a high temperature and in a non-reducing atmosphere, and no substantial change of composition is caused at temperatures of up to about 1700°C. Since there is no prominent difference between a heat treatment temperature higher than 1000°C and a heat treatment temperature of up to 1000°C in connection with the improvement of discharge characteristic or storage characteristic, in production on an industrial scale, in view of equipment such as an electric furnace, the running cost and the operation adaptability, it is preferred that the melting heat treatment of bismuth trioxide be carried out at a temperature in the range of from the melting point (about 820°C) to about 1000°C. Moreover, the organic electrolyte is not limited to those disclosed in the foregoing Examples. For example, solutions formed by dissolving a salt capable of being dissociated into Li⁺ ion, such as LiBF₄, LiPF₆ or LiCF₃SO₃, in an aprotic organic solvent such as γ-butyrolactone, tetrahydrofuran, dioxolane or a mixed solvent thereof can be used as the organic electrolyte. Preferably the organic electrolyte used is a mixed solvent composed mainly of butylene carbonate (hereinafter referred to as "BC") having the following formula: and 1,2-dimethoxyethane (DME), which may further comprise ethylene carbonate (hereinafter referred to as "EC"). A salt soluble in this mixed solvent and capable of dissociating into LI⁺ ions, which does not react directly with the negative lithium electrode or the positive electrode active material, is used as the supporting electrolyte. Salts having a high solubility within a broad temperature range, such as LiClO₄, LiBF₄, LiPF₆ and LiCF₃SO₃, are preferably used. Since the ion conductivity is the highest when the BC/DME mixing ratio is about 1/1, it is especially preferred that the BC/DME mixing ratio be in the range of from 3/1 to 1/3. As is observed with reference to PC, when the mixed solvent of PC and DME is used as the solvent of the organic electrolyte, some decomposition of BC is observed at the terminal stage of the discharge of the cell when the mixed solvent of BC and DME is used as the solvent of the organic electrolyte. The resulting decomposition product reacts with lithium to form a brown reaction product on the surface of the lithium and therefore the internal resistance of the cell is increased and the operating voltage is reduced. Accordingly, in the case where the duration of the discharge of the cell is stopped at a certain cut-off voltage, the effective discharge capacity is slightly reduced and the utilisation of the active material is correspondingly reduced. This reduction depends on the purity of BC, the discharge current, etc. and in general this reduction is not preferred though the reduction is not substantially significant in some mode of the usage of the cell. It was found that when a mixed solvent of BC and DME, to which ethylene carbonate is added, is used, the formation of the brown reaction product on the surface of the lithium at the terminal stage of the discharge is controlled and is hardly observed, and the utilisation ratio of the active material is improved and the discharge capacity is increased. Although the reason why the formation of the reaction product on the surface of the lithium is controlled by the addition of EC has not been completely elucidated, it is presumed that the decomposition of BC is probably controlled by addition to EC. As is seen from the results illustrated in the Example given hereinafter, a sufficient effect is attained by adding EC in an amount of several percent. If the volume ratio of EC exceeds 50%, the solidification point is elevated and the operating temperature range of the cell is narrowed. Accordingly, it is preferred that the amount of EC be smaller than 50%. When the abovementioned mixed solvent composed mainly of BC and DME is used as the solvent of the organic electrolyte, expansion of the cell per a given discharge capacity is much smaller than in the cell comprising the mixed solvent of PC and DME. Accordingly, in a cell comprising the mixed solvent composed mainly of BC and DME, larger quantities of the positive electrode and negative electrode materials can be packed in a given cell space, and the discharge capacity per unit volume can be highly improved. The reason why expansion of the cell on discharge is reduced in an organic electrolyte cell of the present invention has not been completely elucidated. However, it is presumed that the reason is probably as follows. The cell discharge reaction between bismuth trioxide and lithium is represented by the following formula (1) and the reaction products are Bi and Li₂O: 6Li + Bi₂O₃ → 2Bi + 3Li₂O (1) In this reaction, as shown in Table 1, as calculated from the densities and formula weights of Li, Bi₂O₃, Bi and Li₂O, the value of the total volume of Bi and Li₂O per mol of Bi₂O₃ after the cell reaction, calculated from the reaction quantities of formula (1), is smaller than the total volume of Li and Bi₂O₃ before the reaction. However, in the actual discharge of the cell, the cell is expanded. The reason is presumed to be that the reaction product is not formed on the positive electrode so simply as represented by the formula (1) and the reaction is advanced while the electrolyte is included in the reaction product. In fact, when the cell is disassembled after the reaction, it is seen that the electrolyte is substantially absorbed and included in the positive electrode reaction product, and any liquid is hardly observed. Since the solvent of the electrolyte is absorbed and included in the positive electrode reaction product and the positive electrode is hence expanded, it is presumed that the kind and state of the solvent of the electrolyte have serious influences on expansion of the positive electrode by the discharge. EXAMPLE 7 A cell was prepared in the same manner as described in Example 4 except for the electrolyte. As the electrolyte, the following three solutions were used in the present Example: (a) a solution formed by dissolving 1 mol/l of LiClO₄ in a 1/1 volume ratio mixed solvent of BC and DME; (b) a solution formed by dissolving 1 mol/l of LiClO₄ in a 45/50/5 volume ratio mixed solvent of BC/DME/EC; (c) an electrolyte formed by dissolving 1 mol/l of LiClO₄ in a 1/1 volume ratio mixed solvent of PC and DME. The three cells which were the same except for the type of the electrolyte were fabricated by using the foregoing electrolytes, respectively. Each cell had a diameter of 9.5 mm and a height of 3.0 mm. The amount of each electrolyte charged was 45 µl per cell. With respect to each cell, the discharge characteristics under a constant resistance of 7.5 kΩ were determined at 20°C. The obtained results are shown in Figure 7. The discharge capacity was measured to a cut-off voltage of 1.2V and the discharge was carried out under a constant resistance of 7.5 kΩ for 550 hours (at this point, the discharge was completed in all of the cells and the operating voltage was 0V) and the difference in the height between the cell before the discharge and the cell after the discharge was measured. The obtained results are shown in Table 2. As is apparent from the foregoing results, there is no substantial difference between the cell (b) of the present invention and the cell (c) in the discharge capacity attained to the cut-off voltage of 1.2V, but in the cell (b) of the present invention, expansion of the cell by the discharge is much smaller than in cell (c). More specifically, if the maximum height of the cell allowable by the instrument to which the cell is attached is 3.2 mm, a discharge capacity of at least 76 mAh can be taken out of the cell (b) of the present invention. In contrast, in the case of the cell (c), if the discharge capacity exceeds 76 mAh, the cell height increases beyond 3.36 mm, and, therefore, in order to control the cell height to up to 3.2 mm, it is necessary to reduce the quantities of the positive electrode and negative electrode materials by about 10%, and the discharge capacity that can be taken out is correspondingly reduced. In the case of the cell (a), as shown in Figure 7, the internal resistance is increased at the terminal stage of the discharge and the operating voltage is somewhat reduced and, therefore, the discharge capacity attained to the cut-off voltage of 1.2V is slightly smaller than those of the cells (b) and (c). However, the expansion of the cell (a) by the discharge is much smaller than the expansion of the cell (c), as in the cell (b). Accordingly, the capacity per unit allowable volume is much larger in the cell (a) of the present invention than in the cell (c). Furthermore, the fact that the change of shape of the cell is very small is very advantageous for reliability and safety of the instrument to which the cell is attached. Preferably the electrically conductive material for the positive electrode comprises conductive furnace carbon obtained according to the furnace type incomplete combustion method where a natural gas or a gaseous higher hydrocarbon is incompletely burnt in a combustion furnace or in combination with graphite. As a preferred example of the conductive furnace carbon black, a product marketed under the tradename of "Ketjen Black EC" by Akzo is employed. The closed circuit voltage of a cell fabricated by using conductive furnace carbon black as the conductive agent is highly improved over the closed circuit voltage of a cell fabricated by using the same amount of graphite or acetylene black. It is construed that the reason why the closed circuit voltage is improved is that conductive furnace carbon black is excellent over customarily used acetylene black or graphite in the conductivity characteristics when incorporated in the positive electrode material and also in the wettability with an electrolyte and the liquid-absorbing property. In the case where a positive electrode mixture comprising conductive furnace carbon black is compression-moulded into an electrode body having a certain shape, since the mouldability of the electrode mixture is much poorer than the mouldability of the electrode mixture comprising graphite or the like, in order to obtain the mechanical strength necessary for fabrication of a cell, it is preferred that the amount of added conductive furnace carbon black be smaller than 2% by weight. It was found that even if the amount of added conductive furnace carbon black is smaller than 2% by weight, a sufficient conductivity can be obtained. In the case where graphite is used in combination with less than 2% by weight of conductive furnace carbon black, the mechanical strength of the positive electrode moulded body is higher than the mechanical strength obtained when conductive furnace carbon black alone is used and, if necessary, a larger amount of the conductive agent can be added and a higher positive electrode conductivity can be realised. Moreover, as compared with the case where graphite alone is used, the conductivity of the positive electrode is highly improved with a smaller amount of the conductive agent. Accordingly, when conductive furnace carbon black is used, the closed circuit voltage of the cell can be increased and simultaneously, the discharge capacity can be greatly increased by reducing the amount of the conductive agent in the positive electrode and increasing the amount of the positive electrode active material. EXAMPLE 8 Bismuth trioxide powder as the positive electrode active material, Ketjen Black EC powder, acetylene black powder or graphite powder as the conductive agent and a fluororesin as the binder were mixed at weight ratios shown in Table 3, and a predetermined amount of the mixture was packed in a mould and the mixture was compression-moulded into a pellet together with a positive electrode holding ring of stainless steel having an L-shaped section. The moulded body was heated and dried under reduced pressure at 100°C for 10 hours to form a positive electrode. The cell was prepared in the same manner as described in Example 1 except for the electrically conductive material. The cell was subjected to a discharge operation under a constant resistance of 7.5 kΩ. The discharge capacity and the closed circuit voltage at -10°C were measured. The obtained results are shown in Table 4. The final voltage of the discharge capacity was 1.0V, and the closed circuit voltage was measured according to the 7.8 msec pulse method under a load resistance of 2 kΩ. As is apparent from the foregoing results, both the capacity and the closed circuit voltage are greatly influenced by the amount of the conductive agent (acetylene black, Ketjen Black or graphite). In the case of cells F, G and H fabricated by using conductive furnace carbon black (Ketjen Black), a higher closed circuit voltage and a higher discharge capacity can be obtained with a smaller amount of the added conductive agent than in the case of cells A, B and C fabricated by using graphite and cells D and E fabricated by using acetylene black. Furthermore, in the case of the cell I fabricated by using conductive furnace carbon and graphite in combination, the discharge capacity is much higher than in the case of cells C, D and F comprising the same amount of the conductive agent as in cell I, and the close circuit voltage of cell I is slightly lower than that of cell F comprising conductive furnace carbon alone as the conductive agent but there is no substantial difference from the practical viewpoint. The closed circuit voltage of the cell I is apparently higher than that of the cell C comprising graphite alone and the cell D comprising acetylene black alone. In the case of the cell F fabricated by using 2% by weight of conductive furnace carbon black alone as the conductive agent, chipping or breaking is caused at a level of about 10% in the compression-moulding or transfer of the positive electrode pellet. In contrast, this defective level is substantially 0% in the case of the cell I fabricated by using both of conductive furnace carbon black and graphite in a total weight of 2% by weight. Of course, the present invention is not limited to the Examples which are described hereinabove: in particular an organic electrolyte cell which uses the active material in accordance with the present invention can have any other suitable configuration. Additionally, the cell may not have the impregnating member. In this case, the electrolyte is contained in the positive electrode and/or the negative electrode.

Claims: An organic electrolyte cell comprising a negative electrode (2), a positive electrode (5) including a main active material composed of heat treated bismuth trioxide (Bi₂O₃), and an organic electrolyte comprising an organic solvent and a salt dissolved in the organic solvent characterised in that the bismuth trioxide is heat-treated at a temperature above 800°C. A cell as claimed in claim 1, characterised in that the negative electrode (2) comprises lithium as a negative active material and the organic electrolyte comprises the organic solvent and a lithium salt or salts dissolved in the organic solvent. A cell as claimed in claim 1 or 2, characterised in that the bismuth trioxide is heat-treated at a temperature in the range of 800°C to 1000°C in air, an inert gas or vacuum. A cell as claimed in claim 1, 2 or 3, characterised in that the bismuth trioxide is heat-treated at a temperature higher than its melting point. A cell as claimed in claim 1, 2, 3 or 4, characterised in that the bismuth trioxide is subjected to a quenching treatment after heat treatment. A cell as claimed in any preceding claim, characterised in that the positive electrode includes an electrically conductive material. A cell as claimed in claim 6 characterised in that the positive electrode comprises an electrically conductive material and a binder. A cell as claimed in claim 6 or 7, characterised in that the electrically conductive material comprises conductive furnace carbon black produced by the furnace type incomplete combustion method. A cell as claimed in claim 6 or 7 characterised in that the electrically conductive material comprises graphite and conductive furnace carbon black. A cell as claimed in claim 8 or 9, characterised in that the positive electrode contains less than 2% by weight of conductive furnace carbon black. A cell as claimed in any preceding claim characterised in that the organic solvent comprises a mixed solvent composed mainly of butylene carbonate and 1,2-dimethoxyethane. A cell as claimed in claim 11, characterised in that the organic solvent further comprises ethylene carbonate. A cell as claimed in claim 12, characterised in that the amount of ethylene carbonate is less than 50%. A cell as claimed in claim 11, 12 or 13, characterised in that the ratio of butylene carbonate to 1,2-dimethoxyethane is in the range 3/1 to 1/3. A cell as claimed in claim 14, characterised in that the ratio is substantially 1/1. A cell as claimed in any preceding claim, characterised in that the salt is comprised of lithium perchlorate LiCℓO₄.

Inventors: SAKAMOTO, HIDEO C/O SEIKO ELECTRONIC COMPONENTS, TAHARA, KENSUKE C/O SEIKO ELECTRONIC COMPONENTS
Applicants: SEIKO ELECTRONIC COMPONENTS LTD.
Application year: 1987
Main classification: H01M4
IPC codes: H01M6, H01M4