Ternary solvent nonaqueous organic electrolyte for alkali metal electrochemical cells

Abstract: A nonaqueous electrolyte comprising a ternary solvent system preferably including a linear ether mixed with a high permittivity solvent and a low viscosity solvent, is described. This electrolyte is useful for activating an alkali metal/solid cathode electrochemical cell of the kind that typically powers implantable medical devices. The new electrolyte provides improved cell capacity under high current pulse discharge applications while decreasing cell swelling by about 20% in comparison to conventional nonaqueous organic electrolytes consisting of propylene carbonate and dimethoxyethane as the solvents.

Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the conversion of chemical energy to electrical energy, and more particularly, to a nonaqueous electrolyte electrochemical cell. The nonaqueous electrolyte comprises a ternary solvent system including a linear ether solvent mixed with a high permittivity solvent and a low viscosity solvent. 2. Prior Art The widespread use of high energy density alkali metal electrochemical cells is, in part, dependent on the development of highly conductive and stable nonaqueous organic electrolytes. Conventional nonaqueous organic electrolytes suitable for use with alkali metal electrodes are composed of an ion-forming salt, preferably an alkali metal salt with the alkali metal of the salt similar to the alkali metal comprising the electrode, dissolved in a solvent system comprising either a single organic solvent or a mixture of organic solvents. A general requirement of ionaqueous organic electrolytes is their stability toward both the anode and the cathode materials. For high rate alkali metal electrochemical cells such as lithium cells, the use of a highly conductive electrolyte is especially important. To achieve high electrolyte conductivity, the combination of two solvents, one with a high dielectric constant and one with a low viscosity, is generally used Typically highly conductive and stable electrolytes, as disclosed in EPA 0618630, include propylene carbonate (PC) and 1,2-dimethoxyethane (DME). Propylene carbonate has a relatively high dielectric constant of about 64 and is preferably present in conventional electrolytes in an amount of about 10 to 50 volume percent, more preferably about 20 to 30 volume percent. The remainder of the conventional solvent mixture is typically 1,2-dimethoxyethane which functions as a relatively low viscosity solvent. A preferred electrolyte according to the prior art is 1.0M or 1.2M LiAsF 6 in a 50:50 mixture of, by volume, propylene carbonate and 1,2-dimethoxyethane, which has a conductivity of about 17.3 mS. This electrolyte is widely used in the battery industry and its accessful application in a high rate, pulse dischargeable alkali metal/mixed metal oxide defibrillator battery is one of the best examples. In order to minimize the internal resistance during high current density discharge, an electrolyte with improved conductivity over that shown by the prior art electrolytes is desired. However, many electrolytes with improved conductivity (> 17.3 mS) are not suitable for high rate, pulse discharge applications, i.e., for use in implantable medical devices such as a cardiac defibrillator and the like, due to various unfavorable characteristics. These include instability toward the anode, instability toward the cathode, or instability toward both electrodes, poor homogeneity, unacceptable voltage delay, high rate of self discharge and unacceptable cell swelling. The present improved nonaqueous electrolyte for an alkali metal electrochemical cell comprises a ternary solvent system This improved electrolyte not only has high conductivity (> 17.3 mS), but also exhibits good performance characteristics in all other noted categories. U.S. Patent No. 4,952,330 to Leger et al. discloses an alkali metal cell activated with a ternary solvent nonaqueous electrolyte comprising a linear aliphatic ether, a polymerizable component of a cyclic ether, and an alkylene carbonate. While DME and DIPE are both listed as suitable linear aliphatic ethers, this patent specifically teaches use of only one linear aliphatic ether in combination with propylene carbonate as the alkylene carbonate and a cyclic ether such as 1,3-dioxolane. This latter compound is stated as forming a protective film on the anode through reduction of the solvent to suppress the formation of lithium dendrite growth. US Patent No. 5,219,683 discloses a nonaqueous low flammability electrolyte comprising an etherester or a diester. SUMMARY OF THE INVENTION The object of the present invention is, therefore, to improve the performance of an alkali metal electrochemical cell such as a lithium cell by providing an improved nonaqueous electrolyte with high conductivity and good stability. A further object of this invention is to provide such an electrolyte in defibrillator batteries to improve the cell capacity under high current pulse discharge applications and at the same time to minimize the cell swelling characteristics typically associated with such power sources. These and other objects are achieved by using an electrolyte solution for use in an electrochemical cell comprising a ternary, nonaqueous solvent mixture comprising a linear ether as a first, low viscosity solvent, a second, linear ether selected from diethyl ether, ethylpropyl ether, ethyl isopropyl ether, ethylbutyl ether, ethyl tert-butyl ether, dipropyl ether, diisopropyl ether, dibutyl ether, diisobutyl ether, disec-butyl ether, methylpropyl ether, methyl isopropyl ether, methylbutyl ether, methyl secbutyl ether, methyl tert-butyl ether, and mixtures thereof as a second low viscosity solvent and a high permittivity solvent selected from a cyclic carbonate, a cyclic ester, a cyclic amide, dimethyl sulfoxide, acetonitrile, dimethyl formamide, dimethyl acetamide and mixtures thereof. Preferably, the first, low viscosity solvent is present in the solvent mixture at 5 to 20 volume percent. Preferred examples of the first solvent, the second solvent and the high permittivity solvent include 1,2-dimethyoxyethane, diisopropyl ether (RIPE), and propylene carbonate, respectively. In the present invention, the preferred anode is lithium metal and the preferred cathode is a transition metal oxide for example, silver vanadium oxide, Ag 2 V 4 O 11 (SVO) or copper silver vanadium oxide (CSVO). The preferred electrolytes include 1.0M to 1.4 M LiAsF 6 as an ion-forming alkali metal salt dissolved in solvents containing at least one high permittivity solvent such as propylene carbonate and at least one low viscosity solvent, such as 1,2-dimethyoxyethane ether (DIPE) combined with a second low viscosity solvent such as diisopropyl ether (DIPE). BRIEF DESCRIPTION OF THE DRAWING Fig. 1 is a graph showing comparable cell thickness versus potential for lithium/silver vanadium oxide cells activated with various nonaqueous electrolytes according to the prior art and the present invention. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The electrochemical cell of the present invention comprises an anode of a metal selected from Groups IA, IIA or IIIB of the Periodic Table of the Elements, including lithium, sodium, potassium, etc., and their alloys and intermetallic compounds including, for example, Li-Si, Li-Al, Li-B and Li-Si-B alloys and intermetallic compounds. The preferred anode comprises lithium, and the more preferred anode comprises a lithium alloy such as a lithium-aluminum alloy. The greater the amount of aluminum present by weight in the alloy, the lower the energy density of the cell. The form of the anode may vary, but preferably the anode is a thin metal sheet or foil of the anode metal, pressed or rolled on a metallic anode current collector, i.e., preferably comprising nickel, to form an anode component. In the exemplary cell of the present invention, the anode component has an extended tab or lead of the same material as the anode current collector, i.e., preferably nickel, integrally formed therewith such as by welding and contacted by a weld to a cell case of conductive metal in a case-negative electrical configuration. Alternatively, the anode may be formed in some other geometry, such as a bobbin shape, cylinder or pellet to allow an alternate low surface cell design. The cathode is preferably of a solid material and the electrochemical reaction at the cathode involves conversion of ions which migrate from the anode to the cathode in atomic or molecular forms. The solid cathode material may comprise a metal element, a metal oxide, a mixed metal oxide and a metal sulfide, and combinations thereof. The metal oxide, the mixed metal oxide and the metal sulfide can be formed by the chemical addition, reaction, or otherwise intimate contact of various metal oxides, metal sulfides and/or metal elements, preferably during thermal treatment, sol-gel formation, chemical vapor deposition or hydrothermal synthesis in mixed states. The active materials thereby produced contain metals, oxides and sulfides of Groups IB, IIB, IIIB, IVB, VB, VIB, VIIB and VIII, which includes the noble metals and/or other oxide and sulfide compounds. One preferred mixed metal oxide has the general formula SM x V 2 O y wherein SM is a metal selected from Groups IB to VIIB and VIII of the Periodic Table of Elements, wherein x is about 0.30 to 2.0 and y is about 4.5 to 6.0 in the general formula. By way of illustration, and in no way intended to be limiting, one exemplary cathode active material comprises silver vanadium oxide (SVO) having the general formula Ag x V 2 O y in any one of its many phases, i.e., β-phase silver vanadium oxide having in the general formula x = 0.35 and y = 5.8, γ-phase silver vanadium oxide having in the general formula x = 0.74 and y = 5.37 and ∈-phase silver vanadium oxide having in the general formula x = 1.0 and y = 5.5, and combination and mixtures of phases thereof. Another preferred composite cathode material includes V 2 O Z wherein z ≤ 5 combined with Ag 2 O with silver in either the silver(II), silver(I) or silver(0) oxidation state and CuO with copper in either the copper(II), copper(I) or copper(0) oxidation state to provide the mixed metal oxide having the general formula Cu x Ag y V 2 O z , (CSVO). Thus, this composite cathode active material may be described as a metal oxide-metal oxide-metal oxide, a metal-metal oxide-metal oxide, or a metal-metal-metal oxide and the range of material composition found for Cu x Ag y V 2 O z is preferably about 0.01 ≤ x ≤ 1.0, about 0.01 ≤ y ≤ 1.0 and about 5.01 ≤ z ≤ 6.5. Typical forms of CSVO are Cu 0.16 Ag 0.67 V 2 O z with z being about 5.5 and Cu 0.5 Ag 0.5 V 2 O z with z being about 5.75. The oxygen content is designated by z since the exact stoichiometric proportion of oxygen in CSVO can vary depending on whether the cathode material is prepared in an oxidizing atmosphere such as air or oxygen, or in an inert atmosphere such as argon, nitrogen and helium. Additional cathode active materials useful with the present invention include manganese dioxide, lithium cobalt oxide, lithium nickel oxide, copper oxide, titanium disulfide, copper sulfide, iron sulfide, iron disulfide, copper vanadium oxide, fluorinated carbon, and mixtures thereof. Preferably, the cathode comprises from about 80 to about 99 weight percent of the cathode active material. Cathode active materials prepared as described above are preferably mixed with a binder material such as a powdered fluoro-polymer, more preferably powdered polytetrafluoroethylene or powdered polyvinylidene fluoride present at about 1 to about 5 weight percent of the cathode mixture. Further, up to about 10 weight percent of a conductive diluent is preferably added to the cathode mixture to improve conductivity. Suitable materials for this purpose include acetylene black, carbon black and/or graphite or a metallic powder such as powdered nickel, aluminum, titanium and stainless steel. The preferred cathode active mixture thus includes a powdered fluoro-polymer binder present at about 3 weight percent, a conductive diluent present at about 3 weight percent and about 94 weight percent of the cathode active material. The cathode active mixture may be in the form of one or more plates operatively associated with at least one or more plates of anode material, or in the form of a strip wound with a corresponding strip of anode material in a structure similar to a "jellyroll". In order to prevent internal short circuit conditions, the cathode may be separated from the Group IA, IIA or IIIB anode material by a suitable separator material. The separator is of electrically insulative material, and the separator material also is chemically unreactive with the anode and cathode active materials and both chemically unreactive with and insoluble in the electrolyte. In addition, the separator material has a degree of porosity sufficient to allow flow therethrough of the electrolyte during the electrochemical reaction of the electrochemical cell. Illustrative separator materials include fabrics woven from fluoropolymeric fibers including polyvinylidene fluoride, polyethylenetetrafluoroethylene, and polyethylenechlorotrifluoroethylene used either alone or laminated with a fluoropolymeric microporous film, non-woven glass, polypropylene, polyethylene, glass fiber materials, ceramics, polytetrafluoroethylene membrane commercially available under the designation ZITEX (Chemplast Inc.), polypropylene membrane commercially available under the designation CELGARD (Celanese Plastic Company, Inc.) and a membrane commercially available under the designation DEXIGLAS (C.H. Dexter, Div., Dexter Corp.). The electrochemical cell of the present invention further includes a nonaqueous, ionically conductive electrolyte which serves as a medium for migration of ions between the anode and the cathode electrodes during the electrochemical reactions of the cell. The electrochemical reaction at the electrodes involves conversion of ions in atomic or molecular forms which migrate from the anode to the cathode. Thus, nonaqueous electrolytes suitable for the present invention are substantially inert to the anode and cathode materials, and they exhibit those physical properties necessary for ionic transport, namely, low viscosity, low surface tension and wettability. A suitable electrolyte has an inorganic, ionically conductive salt dissolved in a nonaqueous solvent. More preferably, the electrolyte includes an ionizable alkali metal salt dissolved in a mixture of aprotic organic solvents comprising a first, low viscosity solvent, which is a linear ether, a second low viscosity solvent as herein defined and a high permittivity solvent as herein defined. The inorganic, ionically conductive salt serves as the vehicle for migration of the anode ions to intercalate into the cathode active material, and has the general formula MM'F 6 or MM'F 4 wherein M is an alkali metal similar to the alkali metal comprising the anode and M' is an element selected from the group consisting of phosphorus, arsenic, antimony and boron. Examples of salts yielding M'F 6 are: hexafluorophosphate (PF 6 ), hexafluoroarsenate (AsF 6 ) and hexafluoroantimonate (SbF 6 ) while tetrafluoroborate (BF 4 ) is exemplary of salts yielding M'F 4 . Thus, in the case of the anode comprising lithium, the alkali metal salt comprises lithium hexafluorophosphate, lithium hexafluoroarsenate, lithium hexafluoroantimonate or lithium tetrafluoroborate dissolved in a suitable ternary solvent mixture. Alternatively, the corresponding sodium or potassium salts may be used. Other inorganic salts useful with the present invention include LiClO 4 , LiAlCl 4 , LiGaCl 4 , LiC(SO 2 CF 3 ) 3 , LiN(SO 2 CF 3 ) 2 , LiSO 3 F, LiB(C 6 H 5 ) 4 and LiCF 3 SO 3 , and mixtures thereof. Low viscosity solvents useful with the present invention include linear ethers such as diglyme, triglyme, tetraglyme, 1,2-dimethoxyethane (DME) and mixtures thereof, and useful high permittivity solvents include cyclic carbonates, cyclic esters and cyclic amides such as propylene carbonate (PC), ethylene carbonate (EC), acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, γ-butyrolactone (GBL) and N-methyl-pyrolidinone (NMP) and mixtures thereof. Propylene carbonate (PC) is a preferred high permittivity solvent and 1,2-dimethoxyethane is one of the preferred low viscosity solvents of the present invention. In that respect, it is known that electrolyte solvent decomposition contributes to alkali metal/mixed metal oxide cell swelling. For example, in a lithium/silver vanadium oxide (Li/SVO) cell activated with 1.0M LiAsF 6 in a 50:50 percent mixture of, by volume, PC:DME according to the prior art, propene has been found to be the major component of the gaseous products. It is believed that propylene carbonate in the electrolyte is catalytically decomposed to form propene and lithium carbonate according to the following reaction: In general, propene formation is believed to be proportional to the PC concentration. Presumably, propene formation can be reduced during the discharge of an alkali metal/mixed metal oxide electrochemical cell by lowering the percentage of propylene carbonate in the electrolyte. However, only decreasing the percentage of propylene carbonate in the electrolyte has been determined not to help in controlling cell swelling. Instead, the present invention is directed to partially replacing either PC or DME with a second, low viscosity solvent such as a simple, linear ether. Unexpectedly, this results in a decrease in swelling at end-of-life (EOL) of cell discharge by about 20% of the swelling typically experienced in conventional alkali metal electrochemical cells activated with the prior art 50:50 percent mixture of, by volume, PC:DME, no matter what the volume percent of PC is in the electrolyte. Linear ethers useful as the second, low viscosity solvent in the electrolyte of the present invention are diethyl ether, ethylpropyl ether, ethyl isopropyl ether, ethyl butyl ether, ethyl tert-butyl ether, dipropyl ether, diisopropyl ether, dibutyl ether, diisobutyl ether, disec-butyl ether, methylpropyl ether, methyl iso-propyl ether, methylbutyl ether, methyl, secbutyl ether and methyl tert-butyl ether, and mixtures thereof. The most preferred linear ether is diisopropyl ether (DIPE). The present invention is, therefore, generally directed to at least partially replacing PC, DME or both PC and DME with a second, low viscosity solvent, where is a linear ether, the most preferred linear ether being diisopropyl ether, in electrolytes useful for activating alkali metal cells to thereby improve the conductivity of the new electrolyte and concomitantly the cell discharge performance. Thus, propylene carbonate is preferably present in the electrolyte at about 20 to about 50 percent, by volume, and diisopropyl ether as the preferred second, low viscosity solvent is preferably present at about 5 percent .to about 20 percent, by volume, remainder dimethoxyethane. At less than about 5 volume percent, the beneficial effects of DIPE are not pronounced enough to aid in reducing the cell swelling while maintaining high conductivity. Above about 20 volume percent, diisopropyl ether reaches its limit of miscibility, and homogeneity is important in any solvent system. In the present invention, the anode is preferably lithium metal and the preferred electrolyte is 1.0M to 1.4M LiAsF 6 or LiPF 6 dissolved in a ternary aprotic solvent comprising propylene carbonate (PC), dimethoxyethane (DME) and diisopropyl ether (DIPE) in a respective 30:55:15 volume percent mixture. In addition to not compromising discharge performance for the sake of improved conductivity, the ternary solvent electrolytes of the present invention are also stable toward the alkali metal anode and the solid cathode materials as evidenced by heat dissipation measurements. The preferred form of the .electrochemical cell of the present invention is a case-negative design wherein the anode/cathode couple is inserted into a conductive metal casing such that the casing is connected to the anode current collector in a case-negative configuration, as is well known to those skilled in the art. A preferred material for the casing is titanium although stainless steel, mild steel, nickel-plated mild steel and aluminum are also suitable. The casing header comprises a metallic lid having an opening to accommodate the glass-to-metal seal/terminal pin feedthrough for the cathode electrode. The anode electrode is preferably connected to the case or the lid. An additional opening is provided for electrolyte filling. The casing header comprises elements having compatibility with the other components of the electrochemical cell and is resistant to corrosion. The cell is, thereafter filled with the electrolyte solution described hereinabove and hermetically sealed such as by close-welding a stainless steel plug over the fill hole, but not limited thereto. The cell of the present invention can also be constructed in a case-positive design. The following examples illustrate EXAMPLE I Various nonaqueous solvent mixtures comprising propylene carbonate (PC), 1,2-dimethoxyethane (DME) and a linear ether, particularly diisopropyl ether (DIPS), were mixed as listed in Table 1. The ternary solvent electrolytes according to the present invention, i.e., electrolytes 3, 4, 7 and 8 exhibited similar or improved conductivities in comparison to conventional, binary solvent electrolytes 1 and 5. The conductivity of these electrolytes was determined at 37°C. Electrolyte Conductivity Electrolyte [LiAsF 6 ] M [LiPF 6 ] M Solvent Ratio PC:DME:DIPE Conductivity (mmho/cm) 1 1.2 50 : 50 : 0 18.2 2 1.0 50 : 35 : 15 16.7 3 1.2 30 : 55 : 15 18.3 4 1.2 20 : 65 : 15 18.3 5 1.0 50 : 50 : 0 17.3 6 1.0 50 : 35 : 15 16.4 7 1.2 30 : 55 : 15 17.9 8 1.2 20 : 65 : 15 18.2 EXAMPLE II A test group of cells was constructed, each having lithium anode material pressed on a nickel current collector screen and silver vanadium oxide cathode material pressed on an aluminum current collector screen. A prismatic cell stack assembly configuration with two layers of microporous membrane propylene separator sandwiched between the anode and the cathode was prepared. The electrode assembly was then hermetically sealed in a stainless steel casing in a case-negative configuration and the cells were activated with various ones of the electrolytes 1 to 8 set forth in Table 1. In particular, some of the cells in this example, designated as reference cells, were activated with electrolyte 1 and other cells were activated with one of the ternary electrolytes according to the present invention, specifically electrolyte 2 (1.0M LiPF 6 in a 50:35:15 percent mixture of, by volume, PC:DME:DIPE) or electrolyte 3 (1.2M LiPF 6 in a 30:55:15 percent mixture of, by volume, PC:DME:DIPE). All of the cells were subjected to a pre-discharge protocol consisting of a burn-in discharge followed by an acceptance pulse train. During burn-in, a constant resistance load of 2.49 Kohm was applied to the cells to deplete them of approximately 1% of their theoretical capacity. Following burn-in, the cells were acceptance pulse discharged. The pulse train consisted of four 10 second 23.3 mA/cm 2 pulses with 15 second rests between each pulse. The cells were then stored at 37°C for one week. Heat dissipation of these cells was measured by microcalorimetry and the results are listed in Table 2. Following the above pre-discharge protocol, the cells in this example were discharged by applying a pulse train every thirty minutes. The pulse train consisted of four 10 second pulses (23.2 mA/cm 2 ) with 15 second rests between each pulse. The delivered capacities to several voltage limits are also listed in Table 2. Cell Discharge Capacity and Heat Dissipation Electrolyte Heat Dissipation (µ Watt) Capacity (mAh) at Cut Off 2.0V 1.7V 1.5V 1 17.7 1544 1751 1843 2 14.2 1424 1731 1838 3 14.6 1542 1776 1872 After the above tests, these cells were discharged under a 5.1 Kohm resistor until they reached 0.0V. Cell thickness was monitored periodically. The results are presented in Fig. 1. In particular, curve 10 was constructed from the average discharge of the cells activated with the prior art electrolyte 1 comprising a 50:50 percent mixture of, by volume, PC:DME, curve 12 was constructed from the average discharge of the cells activated with the electrolyte according to the present invention comprising a 50:35:15 percent mixture of, by volume, PC:DME:DIPE and curve 14 was constructed from the average discharge of the cells activated with the electrolyte according to the present invention comprising a 30:55:15 percent mixture of, by volume, PC:DME:DIPE. For those cells activated with the ternary solvent electrolytes 2 and 3 according to the present invention, improvements in cell performance are clearly evident in terms of increased stability (low heat dissipation), increased delivered capacity (for electrolyte 3), and decreased cell swelling by about 20% at the EOL of cell discharge in comparison to Li/SVO cells activated with conventional electrolytes, i.e. electrolyte 1. Electrolytes 4 and 8 were not tested because while their conductivity was clearly acceptable, 20 volume percent of propylene carbonate results in an electrolyte having borderline homogeneity. EXAMPLE III Hermetically sealed Li/SVO defibrillator batteries were constructed similar to those described in Example II and were activated with electrolytes 1 and 3, respectively. After being subjected to the pre-discharge protocol consisting of the burn-in discharge followed by the acceptance pulse testing described in Example II, these cells were discharged by applying pulse trains at 37°C once every 8 weeks over a 17.4 Kohm background load. The pulse trains consisted of four 10 second pulses (23.2 mA/cm 2 ) with 15 second rests between each pulse. The pulse voltages in each pulse train are listed in Table 3 wherein Pprel indicates the voltage before the application of the pulse train, Plmin indicates the minimum voltage during the first pulse of the pulse train, P4min indicates the minimum voltage of the fourth pulse of the pulse train and Plmin - P4min is calculated from the minimum voltage of the first pulse minus the minimum voltage of the fourth pulse of the pulse train. For those cells activated with electrolyte 3 (1.2M LiPF 6 in a 30:55:15 percent mixture of, by volume, PC:DME:DIPE), the pulse minimum potentials are higher than those of the control cells activated with electrolyte 1 (1.2M LiPF 6 in a 50:50 percent mixture of, by volume, PC:DME). In addition, cells with electrolyte 3 also had a lower polarization voltage drop as indicated by the pulse 1 minimum minus the pulse 4 minimum (P1min - P4min) presented in the last column of Table 3. Cell Discharge Potentials Pulse Train Electrolyte Ppre1 (V) P1min (V) P4min (V) P1min-P4min 1 1 3.238 2.713 2.565 0.148 3 3.241 2.718 2.593 0.125 2 1 3.184 2.633 2.476 0.157 3 3.188 2.640 2.507 0.133 3 1 2.980 2.504 2.388 0.116 3 2.985 2.517 2.417 0.100 4 1 2.740 2.357 2.297 0.060 3 2.740 2.368 2.317 0.051 5 1 2.573 2.211 2.195 0.016 3 2.573 2.240 2.224 0.016 6 1 2.529 2.116 2.088 0.028 3 2.529 2.162 2.134 0.028 EXAMPLE IV Instead of using aluminum cathode current collector screens, titanium cathode screens were used in this example. The hermetically sealed cells in this example were assembled in a similar manner as the cells described in Example II except that some cells, designated as reference cells, were activated with electrolyte 5 (1.0M LiAsF 6 in a 50:50 percent mixture of, by volume, PC:DME) while the remaining test cells were activated with electrolyte 7 (1.2M LiAsF 6 in a 30:55:15 percent mixture of, by volume, PC:DME:DIPE). After being subjected to the pre-discharge protocol consisting of the burn-in discharge followed by the acceptance pulse testing described in Example II, the cells in this example were discharged by applying pulse trains at 37°C over 11.0 Kohm and 17.4 Kohm background loads, respectively. The pulse trains consisted of four 10 second pulses (18.4 mA/cm 2 ) with 15 second rests between each pulse. The resulting pulse voltages are listed in Table 4. Cell Discharge Potentials* Load (Kohm) Electrolyte Ppre1 (V) P1min (V) P4min (V) P1min-P4min 11.0 5 3.217 2.622 2.584 0.038 7 3.217 2.657 2.626 0.031 17.4 5 3.225 2.654 2.608 0.046 7 3.225 2.672 2.643 0.029 For those cells activated with electrolyte 7 according to the present invention, the improvement in cell performance is clearly evident in terms of higher pulse minimum potentials and lower polarization voltage drop during high current pulse discharge while exhibiting excellent conductivity. From the above examples, it is clearly demonstrated that ternary solvents according to the present invention containing a high permittivity solvent such as PC, a first, low viscosity solvent such as DME and a second, low viscosity solvent comprising a linear ether (DIPE for example) present several advantages over the conventional PC/DME binary solvent system. These include stability in the form of lower heat dissipation (Table 2), decreased cell swelling at EOL (Fig. 1), higher pulse minimum voltage (Tables 3 end 4), and lower polarization voltage drop during pulse discharging (Tables 3 and 4).

Claims: An electrolyte solution for use in an electrochemical cell comprising a ternary, nonaqueous solvent mixture comprising a linear ether as a first, low viscosity solvent, a second, linear ether selected from diethyl ether, ethylpropyl ether, ethyl isopropyl ether, ethylbutyl ether, ethyl tert-butyl ether, dipropyl ether, diisopropyl ether, dibutyl ether, diisobutyl ether, disec-butyl ether, methylpropyl ether, methyl isopropyl ether, methylbutyl ether, methyl secbutyl ether, methyl tert-butyl ether, and mixtures thereof as a second low viscosity solvent and a high permittivity solvent selected from a cyclic carbonate, a cyclic ester, a cyclic amide, dimethyl sulfoxide, acetonitrile, dimethyl formamide, dimethyl acetamide and mixtures thereof. The electrolyte solution of Claim 1 wherein the first, low viscosity solvent is present in the solvent mixture at 5 to 20 volume percent. The electrolyte solution of Claim 1 or 2 wherein the electrolyte includes an alkali metal salt dissolved therein. The electrolyte solution of Claim 3 wherein the alkali metal salt has the general formula MM 1 F 6 or MM 1 F 4 and wherein M is an alkali metal and M 1 is an element selected from phosphorus, arsenic, antimony and boron. The electrolyte solution of Claim 3 or 4 wherein the alkali metal salt is selected from LiPF 6 , LiAsF 6 , LiSbF 6 , LiBF 4 , LiClO 4 , LiAlCl 4 , LiGaCl 4 , LiC(SO 2 CF 3 ) 3 , LiCF 3 SO 3 , LiSO 3 F, LiB(C 6 H 5 ) 4 and mixtures thereof. The electrolyte solution of any one of Claims 1 to 5 wherein the high permittivity solvent is selected from propylene carbonate, ethylene carbonate, γ-butyrolactone, N-methyl-pyrrolidinone, dimethyl sulfoxide, acetonitrile, dimethyl formamide, dimethyl acetamide and mixtures thereof. An electrolyte solution according to Claim 1 comprising propylene carbonate, dimethyoxyethane and diisopropyl ether. The electrolyte solution of Claim 7 wherein the propylene carbonate, dimethoxyethane and diisopropyl ether are present in a ratio of about 3:5.5:1.5, by volume, respectively. A system comprising an electrochemical cell and an electrolyte solution, the electrochemical cell comprising: a. an anode comprising an alkali metal; b. a cathode comprising a cathode active material; and c. an electrolyte solution according to any one of Claims 1 to 8 said solution activating the anode and the cathode. The electrochemical cell of Claim 9 wherein the anode comprises either lithium or a lithium-aluminum alloy. The electrochemical cell of Claim 9 or 10 wherein the cathode is comprised of the cathode active material selected from silver vanadium oxide, copper silver vanadium oxide, manganese dioxide, lithium cobalt oxide, lithium nickel oxide, copper oxide, copper sulfide, iron sulfide, iron disulfide, fluorinated carbon, titanium disulfide, copper vanadium oxide and mixtures thereof. The electrochemical cell of any one of Claims 9 to 11 wherein the cathode active material comprises from 80 to 99 weight percent of the cathode. The electrochemical cell of any one of Claims 9 to 12 wherein the cathode further comprises a binder material and a conductor additive. The electrochemical cell of Claim 13 wherein the binder material is a fluoro-resin powder. The electrochemical cell of Claim 13 wherein the conductive additive is selected from carbon, graphite powder, acetylene black and metallic powder selected from titanium, aluminum, nickel, stainless steel and mixtures thereof. The electrochemical cell of any one of Claims 9 to 15 wherein the cathode is comprised of 0 to 3 weight percent carbon, 1 to 5 weight percent of a powder fluoro-resin, the balance being cathode active material. An electrochemical cell according to any one of Claims 9 to 16 wherein the cathode includes, as cathode active material, a mixed metal oxide comprised of vanadium oxide and a second metal "SM" of Group IB of the Periodic Table of Elements, the mixed metal oxide having the general formula SM x V 2 O y wherein 0.3 ≤ x ≤ 2.0 and 4.5 ≤ y ≤ 6.0. An electrochemical cell, according to any one of Claims 9 to 16 wherein the cathode includes, as cathode active material, a mixed metal oxide comprised of vanadium oxide and a mixture of copper and a second metal "SM" of Group IB of the Periodic Table of Elements, the mixed metal oxide having the general formula Cu x SM y V 2 O z wherein 0.01 ≤ x ≤ 1.0, 0.01 ≤y ≤1.0 and 5.01 ≤ z ≤6.5. The electrochemical cell of Claim 18 wherein x ≤ y. An implantable medical device including an electrochemical cell in accordance with any one of Claims 9 to 19. A method of providing an electrochemical cell activated with a nonaqueous electrolyte, comprising the steps of: a. providing a casing; b. providing an anode comprising an alkali metal; c. providing a solid cathode comprising a cathode active material, wherein the anode and the cathode are disposed inside the casing in electrical association with each other; and d. activating the anode and the cathode with the nonaqueous electrolyte of any one of Claim 1 to 8.

Inventors: GAN HONG, TAKEUCHI ESTHER S, GAN, HONG, TAKEUCHI, ESTHER S.
Applicants: GREATBATCH W LTD, WILSON GREATBATCH LTD.
Application year: 1997
Main classification: H01M6
IPC codes: H01M4, H01M6