Glass sealing materials for sodium-sulfur batteries and batteries made therewith

Abstract: A glass composition having a composition between about 18 and about 23 mole % Na₂0, about 3 to about 7 mole % Cs₂0, the balance being B₂0₃ is adaptable to match the thermal expansion coefficient of a beta''-Al₂0₃ solid electrolyte when used to bond and seal the solid electrolyte to a porous support plate (22) in a sodium-sulfur battery (10).

Description: The present invention relates generally to advanced technology thermal battery systems. More particularly, the present invention relates to sodium-sulfur thermal batterics for use in providing a high-power density electrical energy source and most particularly it relates to improved glass sealing systems used in such batteries. The sodium-sulfur battery was first introduced in the mid 1960's. Since that time, there has been a great deal of interest in developing cell designs which are suitable for a wide variety of applications. Batteries which have been under development include those for use in automobiles and train locomotives. One such battery is described by Frank A. Ludwig in U.S. Patent 4,977,044, the teachings of which are incorporated herein in its entirety. Cell designs have also been investigated for producing batteries for storage of electricity for delayed use in order to level out the production rate of electricity and for space systems requiring high energy density. The sodium-sulfur battery is used as a secondary, that is, rechargeable battery. Its use as a primary (onetime discharge) battery would be unwarranted because of the cost, complexity and fragility involved in edge-sealing and incorporating a ceramic solid electrolyte into a battery design. In addition, there are other relatively inexpensive primary batteries of higher power density available in the marketplace. Sodium-sulfur thermal batteries typically include a molten sodium electrode, a molten sulfur electrode and a relatively thin sheet of a solid ceramic sodium ion conducting electrolyte which serves as a separator between the sodium and sulfur electrodes. The electrolytic reaction occurs when sodium ions diffuse through the separator to react with the molten sulfur. Consequently, an important requirement for the separator is that it has a sufficiently high rate of diffusion for sodium ions to allow, during initial operation of the thermal battery, the formation of a sodium polysulfide electrolyte within the separator. To provide satisfactory mechanical strength for the thin ceramic sheet separators used in such a structure, it is typically bonded to an underlying support plate comprised of a porous material such as graphite or fused titania. The sodium-sulfur cell usually operates at a relatively high temperature (300-400°C) in order to maintain not only the sulfur and sodium, but also their reaction products, in a molten state. It is believed that the migration of sulfur and sodium into the porous separator occurs when the cell is heated to operating temperatures for the first time to produce a polysulfide gradient. This polysulfide gradient is composed of sodium sulfides having the formula Na₂S x wherein x is approximately five or less but greater than or equal to one. The composition of the gradient is believed to be: Na₂S/Na₂S₂/Na₂S₃/Na₂S₄/Na₂S₅ Na₂S is a solid at temperatures below 1000° C. As a result, the solid Na₂S acts as a barrier which prevents migration of liquid sulfur or sodium through the entire porous separator. At the same time, the remainder of the polysulfide gradient provides levels of ionic conductivity which are not possible with the previous solid ceramic materials. The use of a porous separator in combination with a polysulfide gradient provides suitable liquid electrode separation while also providing high rates of ionic conduction and resulting high electrical power output. In use, it is found that a structure as described herein above reduces the electrical resistance of the sodium-sulfur cell, leading to low I²R power losses and, therefore, high delivered power densities from the battery's cells. In this structure, the porous support structure, by supporting the ceramic separator, allows the use of a separator sheet that would otherwise be too thin to survive the thermal and mechanical stress generated during operation of the cell. At the same time, the porous separator permits sodium to diffuse therethrough and contact the inner side surface of the alumina, so that the cell reaction can occur. The solid electrolyte is a critical part of the cell configuration because it must provide separation of the liquid sodium from the liquid sulfur in order to prevent catastrophic cell failure. One widely used solid electrolyte in sodium-sulfur batteries is beta"-(double prime) alumina. To improve the bonding between the solid alumina electrolyte and the underlying porous support, one or more glass compositions may be used to join the two materials and seal the edges of the bond line. To be effective, the glass must be able to wet both of the materials and be chemically compatible with the corrosive and high temperature environment of the cell. It must also have a coefficient of thermal expansion which is close (if not identical) to that of the thin and fragile solid alumina electrolyte and also have a viscosity low enough, when molten, to allow fusion to both the porous support and the solid alumina electrolyte at a relatively low processing temperature and yet have a melting point which is high enough to resist deformation over the lifetime of the cell. At the present time, no glass composition available satisfactorily meets all of these requirements. US-A-4311772 and its divisional US-A-4347295 describe sealing glasses for use in electrochemical, electrical, electronic and optical applications. The sealing glasses consist essentially of 3-30% R₂O and 60-95% B₂O₃, wherein R₂O consists of K₂O, Rb₂O, Cs₂O and mixtures thereof. The sealing glasses optionally contain up to 20% of Na₂P and up to 10% SiO₂. The above percentages are calculated in mole percent on the oxide basis. The sealing glasses are especially suitable for forming a seal to sodium glass membrane electrolytes in sodium-sulfur batteries. EP-A-0453796, which was published after the priority date but before the filing date of the present application, describes composite ion-conducting separators for sodium-sulfur batteries. The separators comprising a first layer of solid sodium-ion electrolyte, such as beta-alumina, and a second, porous, electronically conductive support layer bonded to the first layer. The second layer may be formed from graphite or porous titanium dioxide. The layers are bonded together by means of an electrophoretic deposition process, a chemical vapor deposition process, a plasma spraying deposition process, a pyrolytic deposition process, a pressing and sintering process or a glass frit bonding process. The glass frit bonding processes using sealing glass compositions as disclosed in US-A-4347295. The present invention provides a glass composition for bonding and sealing a solid electrolyte to a porous separator in a sodium-sulfur battery, said composition consisting essentially of 18-23 mole % Na₂O, 4-6 mole % Cs₂O and the balance B₂O₃. The present invention also provides a separator for use in a sodium-sulfur battery, comprising a solid electrolyte; a glass seal, wherein the glass consists essentially of from 18-23 mole % Na₂O, 4-6 mole % Cs₂O and the balance B₂O₃; and a porous support plate, wherein the glass seal bonds and seals the solid electrolyte to the porous support plate. The present invention further provides a method of sealing a separator for a sodium-sulfur battery, comprising the steps of: providing a solid electrolyte; depositing a sealing glass on the electrolyte, wherein the glass consists essentially of 18-23 mole % Na₂O, 4-6 mole % Cs₂O and the balance B₂O₃; providing a porous support plate on the sealing glass; and heating the assembled structure so as to fuse the glass to the solid electrolyte and the support plate. The glass composition used to seal the separator is chemically compatible with the corrosive and high temperature environment in a cell of a sodium-sulfur battery. It has a composition consisting essentially of between 18 and 23 mole % Na₂O, 4 to 6 mole % Cs₂O, with the balance being B₂O₃. Glass compositions according to this formula may be readily fine tuned to provide close to an exact match to the thermal expansion coefficient of the thin and fragile beta''-Al₂O₃ electrolyte. these glass compositions also have viscosities that are low enough so that they can be fused to the beta''=Al₂O₃ and the porous support at a relatively low processing temperature, and melting points high enough to resist deformation over the lifetime of the cell at high temperature. The separators of the present invention make it possible to construct a very high power density battery. The total savings in the cost and weight of an electric vehicle's battery system, for example, may make electric vehicles viable in the market place. In addition, other applications of this battery system where battery size and weight are important will be benefited. The various features and advantages of the present invention may be more readily understood with reference to the following detailed description taken in conjunction with the accompanying drawings, wherein like reference numerals designate like structural elements, and in which: Figs. 1 and 2 show side and top views of an exemplary sodium-sulfur battery constructed using the glass composition of the present invention; Fig. 3 is a graph showing the thermal expansion coefficients of alkali-borate glasses; and Fig. 4 is a graph showing the curves for calculating Na₂O to Cs₂O ratios to provide the glass composition of the present invention. Figs. 1 and 2 show side and top views of an exemplary sodium-sulfur battery 10 constructed using the separator of the present invention. As shown therein the cell 10 includes a metal wick anode 12 which is impregnated with metallic sodium and a carbon graphite felt cathode 14 which is impregnated with sulfur. The anode 12 and cathode 14 are separated by a porous oxide separator 16. Current collectors 18 and 20 are provided at the anode 12 and cathode 14, respectively, for allowing removal of electrical energy from the cell 10. Bonded to the sodium side of the separator 16 is porous support plate 22. This serves to reinforce the separator with the porosity thereof being of sufficient size and quantity so as not to significantly impede the passage of liquid or gaseous sodium making contact with the electrolyte containing ceramic separator 16. The top and bottom surfaces of the assembly are then sealed with glass 24, a top view of said seals being shown as Fig. 2. The material used to form the metallic wick anode 12 may be any known material that preferentially wets sodium metal. These materials include nickel, steel, or any other suitable metallic material. Preferably the wick anode 12 is made from nickel felt which is commercially available. The pore size and surface area of the nickel felt may be varied provided that sufficient wetting and impregnation with sodium metal is possible in order to form a suitable liquid electrode. Nickel felt suitable for this application is marketed under the trade name Fibrex by the National Standard Company, Niles, Michigan. The wick anode 12 or felt cathode 14 utilized to support the liquid sulfur may be any conductive fibers, powders or felt materials which are preferentially wet by molten sulfur. Commercially available graphite felts are the materials of choice in state-of-the-art sodium-sulfur battery technology. Any of the felts used in these batteries is adequate for the purposes of the present invention. An adequate felt is SGF available from Stackpole Corp., St. Marys, Pennsylvania. The porous material used for the separator 16 should have sufficient porosity to allow preliminary migration of fluid (liquid or gaseous) sodium metal and fluid (liquid or gaseous) sulfur therethrough during initial operation of the battery to form the initial polysulfide electrolyte gradient. In the present invention, the term "preliminary migration" is used to denote that migration which occurs upon initial operation of the cell, in order to establish the polysulfide electrolyte gradient across the solid electrolyte. Once this gradient is established, there is no longer a free flow of the fluids; however, the gradient established is sufficient to promote diffusion through the separator 16. The porous separator 16 can be made from a ceramic material such as silica fibers sintered into a porous mat such as is available from Lockheed Corp., Sunnyvale, California as FRCI-12 or HTP-12. Other suitable porous ceramic materials include zirconia or alumina felt and paper available from Zircar Products, Inc., Florida, New York. with Zircar alumina felt and paper APA-1, APA-2 and APA-3 being preferred. Especially preferable is beta'' alumina which is available from Ceramatec (USA), Brown-Boveri (Switzerland) or NKG (Japan). As shown in Figs. 1 and 2, the assembly of the separator 16 with the porous support plate 22 is typically accomplished by the use of a sealing glass 24 which, in the preferred embodiment performs two separate functions and is in two different places. In the first of these, the glass forms a plurality of short supporting seal glass pedestals 26 which, in a subsequent fusion process, melt and form a mechanically strong bond between the ceramic top separator 16 and the underlying graphite support plate 22 below. In the second place the glass is formed as a continuous band 28 around the circumference of the battery 10. Sealing and bonding occur when the glass is heated beyond its fusion temperature, as will be described herein below. In the structural embodiment shown, the porous support plate 22 supports the separator 16 while allowing sodium ions to diffuse through it to come in contact with the inner surface thereof. Any thermally stable porous material able to resist the environment of an operating sodium-sulfur cell may be used for this purpose. Typical subport materials used for this purpose are graphite and fused titania. In providing a finished structure having the requisite electrical, thermal and mechanical properties, the glass 24 used to bond the separator 16 to the graphite support plate 22 must have a thermal expansion coefficient, viscosity, and overall chemical inertness which closely match those of the ceramic separator. The present invention uses a glass composition that can be fine tuned to closely match the thermal expansion coefficient of a solid, thin beta''-Al₂0₃ electrolyte. The value of the thermal expansion coefficient for this material is about 7.8 x 10⁻⁶ cm/cm/°C. It has been found that glass compositions comprising Na₂O·Cs₂O and B₂0₃, wherein the glass consists essentially of between 18 and about 23 mole % Na₂O, 4 to 6 mole % Cs₂O, with the balance being B₂O₃, have the necessary chemical resistance to the hostile cell environment and, further, offer the ability to fine tune the thermal expansion coefficient of the glass to a desired value, as discussed above. Preferably, the glass comprises between 19 and 21 mole % Na₂O and 4 to 6 mole % Cs₂O, with the B₂O₃ being 75 mole% of the total glass composition. In fine tuning the composition to meet a particular need, it is found that the key determinants are the viscosity and coefficient of thermal expansion. The viscosity of borate glasses having a genes composition as defined above varies monotonically, and approximately linearly, with A₂O, the total alkali oxide content (in mole %), wherein A is LI, Na, K, Rb, Cs or Fr, of the finished glass. The thermal expansion coefficient varies with composition in a complex way, as shown in Fig. 4 which is taken from a paper written by D. R. Uhlman and R. R. Shaw published in the Journal of Non-Crystalline Solids (1, 347 (1969)). Fig. 4. shows the dependance of the thermal expansion coefficient of alkali borate glasses as a function of their alkali oxide content. As plotted therein, the possible thermal expansion coefficients for alkali borate glasses containing only one alkali metal species are limited to points on the curve associated with that alkali metal species. For such a glass composition, if one chooses a total mole % alkali oxide to provide the desired viscosity in the finished glass, only one value for the thermal expansion coefficient is possible. On the other hand, if one chooses the desired thermal expansion coefficient, only one or, at most, two alkali oxide compositions are possible. As a result, with glasses containing only one alkali metal oxide species, it would be entirely coincidental if the desired values of both viscosity and thermal expansion coefficient were obtained in the same glass composition. The possibilities for so doing are further limited by the fact that lithium and potassium containing glasses cannot be used because these metals are readily leached from the glass by the liquid sodium. Furthermore, the use of rubidium and francium containing glasses is limited by their scarcity and cost. Therefore, for all practical purposes only sodium and cesium containing borate glasses can be considered as being useful for sodium-sulfur battery applications. A modification of Fig. 4, showing just the effects of sodium and cesium is shown as Fig.5. For the purposes of illustration let us assume that a glass with the optimum viscosity for processing and use contains 25 mole% alkali oxide. An analysis of the data from Fig. 4, as depicted in Fig.5, shows the optimum or most preferred composition to be: 19.6 mole% Na₂0, 5.4 mole% Cs₂0, and 75.00 mole% B₂0₃. The glass composition has been designed specifically so that the percentages of the two alkali oxide constituents can be varied to provide a more-or-less an exact match to the thermal expansion coefficient of beta''-Al₂0₃. The glass also has a sufficiently high viscosity at about 350°C that it will not flow or creep during the lifetime of the cell. If a thermal expansion coefficient that is intermediate between those of beta''-Al₂0₃ and TiO₂ is desired, this can be achieved by altering the Na₂0 to Cs₂0 ratio as described above, while maintaining constant viscosity by holding the total alkali oxide content of the glass (Na₂0 + Cs₂0) constant. If a higher or lower viscosity is desired, this can be achieved by altering the total alkali oxide content of the glass, while maintaining a constant thermal expansion coefficient by holding the Na₂0 to Cs₂0 ratio constant. The ability to fine tune the glass to provide the optimum expansion coefficient, while staining the desired viscosity, is a desirable feature of this invention. The glass imposition may be prepared by mixing powders of sodium metaborate, boric acid, sodium carbonate, and cesium carbonate in the correct ratios to obtain the above composition, melting the mixture in a glass-making muffle furnace at high temperature using a platinum or zirconium crucible. Homogenization is achieved by occasional stirring or by bubbling O₂ through the melt using a platinum tube. The glass is then poured out onto graphite to cool. Particularly for application to fused titania, it is most convenient to use standard screen printing techniques to apply the glass in a pattern as shown in Figure 2. For this purpose, the glass is ground into a powder of suitable particle size distribution, and made into a paste using an anhydrous organic liquid such as cumene, toluene or benzene as a vehicle, and a polymeric or high molecular weight organic material such as alpha methyl polystyrene as a binder. Suitable materials include those that do not absorb appreciable water from the atmosphere, and those that burn off cleanly during the process of fusing the glass powder to make the seal. A number of these materials are well known to those skilled in screen printing of glass powders or glass-containing metallizations. Since all borate glasses are highly hygroscopic, the glass should be prepared, ground, and subsequently handled under controlled and reduced humidity conditions. But, because beta''-Al₂0₃ is also hygroscopic, this condition should pose no special requirements on the battery assembly process. After screen printing the glass onto the titania support in the appropriate pattern, the beta''-Al₂0₃ sheet is placed upon the glass, and the assembly is fired in a vacuum furnace to volatilize the organic species, melt and fuse the glass powder, and form a tight seal between the beta''-Al₂0₃ and the TiO₂. The structure should be cooled from fusing temperature to room temperature gradually, preferably at a rate of around 1°C/min for the temperature range between the softening point and the strain point of the glass. At lower temperatures, it may be cooled at faster rates. Thus there has been described new and improved separators for use in sealing sodium-sulfur batteries. It is to be understood that the above-described embodiment is merely illustrative.

Claims: A glass composition for bonding and sealing a solid electrolyte to a porous separator in a sodium-sulfur battery, said composition consisting essentially of 18-23 mole % Na₂O, 4-6 mole % Cs₂O and the balance B₂O₃. The glass composition of claim 1 wherein the B₂O₃ comprises about 75 mole % of the composition. The glass composition of claim 2 wherein the composition contains 19-21 mole % of Na₂O. A separator for use in a sodium-sulfur battery, comprising a solid electrolyte; a glass seal, wherein the glass consists essentially of 18-23 mole % Na₂O, 4-6 mole % Cs₂O and the balance B₂O₃; and a porous support plate, wherein the glass seal bonds and seals the solid electrolyte to the porous support plate. The separator of claim 4 wherein the solid electrolyte comprises beta''-Al₂O₃ and the porous support plate is formed of a material selected from the group consisting of graphite and fused titania. A method of sealing a separator for a sodium-sulfur battery, comprising the steps of: providing a solid electrolyte; depositing a sealing glass on the electrolyte, wherein the glass consists essentially of 18-23 mole % Na₂O, 4-6 mole % Cs2O and the balance B₂O₃; providing a porous support plate on the sealing glass; and heating the assembled structure so as to fuse the glass to the solid electrolyte and the support plate. The method of claim 6 wherein the solid electrolyte comprises beta''-Al₂O₃ and the porous support plate is formed of a material selected from the group consisting of graphite and fused titania.

Inventors: MEGERLE CLIFFORD A, MEGERLE, CLIFFORD A.
Applicants: HUGHES AIRCRAFT CO, HUGHES AIRCRAFT COMPANY
Application year: 1992
Main classification: C03C8
IPC codes: H01M2, C03C8, C03C3, H01M10