ELECTROCHEMICAL CELL CONSTRUCTIONS AND METHODS OF MAKING THE SAME

Abstract: A method of making electrochemical cells with high anode-to-cathode interfacial surface area and improved discharge efficiency at high rate discharge, without sacrificing total capacity involves the use of a separator coated electrode, and a flowable material comprising a second electrode. The first electrode and flowable material comprising the second electrode are disposed in a cell housing. The flowable material surrounds the coated surfaces of the first electrode. The invention also provides simplified methods for making electrochemical cells having a high anode-to-cathode interfacial surface area.

Description: ELECTROCHEMICAL CELL CONSTRUCTIONS AND METHODS OF MAKING THE SAME This invention relates to the field of electrochemical cells, and more particularly to electrochemical cells having very high anode-to-cathode interfacial surface area and, therefore, high rate discharge efficiency. Electrochemical cells are commonly employed to supply voltage for electrically operated devices, and particularly for portable electrically operated devices. Popular alkaline cells of the generally cylindrical type are commercially available in industry standard sizes including D-, C-, AA-, AAA-, and AAAA-size cells. There is an increasing demand for alkaline cells, particularly alkaline cells of the commonly commercially available sizes, which exhibit improved discharge efficiency at high discharge rates. A frequently used configuration for high discharge rate batteries is a spiral wound electrode assembly, also known as a jelly-roll type assembly, in which a positive electrode, a negative electrode, and a separator sheet, are spirally wound to provide a high surface area between the electrodes, whereby a high discharge rate is achievable. The spiral wound construction requires that the electrodes be provided with a separator to avoid shorting. If conventional separators, such as paper or cellulose separators, are used, typically approximately 10% to 20% of the total volume of a AA-size jelly-roll cell with a 1 10 square centimetre anode-to-cathode surface area is consumed by non- active separator material. The increased interfacial surface area results in increased high rate capacity. However, the reduction in active material volume causes reduced capacity at low rates of discharge. If the current separator could be replaced with a thinner separator, spirally wound electrode configurations and alternative cell constructions could be provided which produce an alkaline cell with higher interfacial surface area and increased high rate performance Another disadvantage with conventional spiral wound cell constructions is that the machines used for spirally winding two electrodes and a separator are relatively expensive to fabπcate, operate and maintain Accordingly, improved methods and cell constructions are desired US-A-5, 869,205 discloses an electrochemical cell having multiple anode compartments to increase anode-to-cathode interfacial area One embodiment includes a first electrode disposed in a container, in which the first electrode includes four cyhndπcally shaped cavities, with a second electrode disposed within each of the four cavities A conventional separator is disposed within each of the four cavities While the cell configuration described in US-A-5, 869, 205 achieves a substantial improvement in high rate capacity, conventional separators are used Accordingly, the improved discharge efficiency at high discharge rates, which is associated with an increase in anode-cathode interfacial surface area, is also accompanied by a proportional increase in separator area and separator volume Therefore, improved discharge efficiency at high discharge rates is achieved, at least in part, by sacrificing total capacity It would be desirable to achieve even greater improvements in discharge efficiency at high discharge rates, and preferably to achieve such improvements without sacrificing total capacity US-A-3,156,585 discloses a hermetically sealed storage battery comprising a plurality of concentrically arranged ring-shaped electrodes, each of which is separated from an adjacent electrode by a conv entional separator Although the patent does not specifically mention improved discharge efficiency at high discharge rates, the battery construction shown would be expected to have an increased anode-to-cathode interfacial surface area, and would be expected to exhibit at least some improvement in discharge efficiency at high discharge rates However, the battery structure is extremely complicated, and would be difficult to manufacture at a competitive price Any improvement in discharge efficiency at high discharge rates would be accompanied by a significant increase in separator area and volume and, therefore, a significant decrease in total capacity. It would be desirable to provide alkaline cells having increased anode-to- cathode interfacial area, and which are simpler in design and, therefore, less expensive, and which preferably achieve improved discharge efficiency at high discharge rates without sacrificing total capacity. US Serial No. 09/198,802, filed 24 November 1998, discloses a high rate electrochemical cell comprising a first electrode of a first polarity disposed in a container, a second electrode of a second polarity disposed on one side of the first electrode, a first current collector disposed in contact with the first electrode, and an outer electrochemically active layer having the second polarity and being disposed on another side of the first electrode. A separator is disposed between the first electrode and the second electrode and between the second electrode and the outer electrochemically active layer. The construction disclosed in US Serial No. 09/198,802 has the advantage of achieving a substantial increase in anode-to-cathode interfacial surface area, and hence an improvement in discharge efficiency at high discharge rates, using a relatively simple design which can be produced at a competitive price. However, because the separator between the first and second electrode and between the second electrode and the outer electrochemically active layer is a conventional separator, the improved discharge efficiency at high discharge rates is accompanied with an increase in separator volume, and, therefore, a decrease in total capacity. The invention pertains to batteries having high anode-to-cathode interfacial surface area, and improved discharge efficiency at high discharge rates. The invention also provides methods for making batteries having high anode-to-cathode interfacial surface area, and improved discharge efficiency at high discharge rates. The batteries and methods of this invention generally involve the use of a first electrode or electrode material which is provided with a coating that functions as a separator, and the use of a flowable electrode material which flows around and contacts the coated electrode. Accordingly, in a first lspect, the present invention provides a battery comprising: a housing; a first electrode disposed in the housing; a coating which functions as a separator, the coating located on a surface of the first electrode; and a flowable second electrode material, the flowable second electrode material disposed in the housing and surrounding the coated surface of the first electrode . In a second aspect, the present invention provides a method of making a battery comprising: providing a housing; providing a first electrode; forming on a surface of the first electrode a coating which functions as a separator; disposing the coated first electrode in the housing; and disposing a flowable material in the housing, the flowable material including a second electrode material, the flowable material surrounding the separator coated on the surface of the first electrode. The expression "flowable electrode material" refers to an electrode material having the ability to flow around and completely surround a solid electrode. Such materials generally comprise a mixture of a liquid electrolyte and dispersed solid particles of an electrochemically active material. The flowable electrode may be a low viscosity material such as a liquid or a relatively high viscosity material such as a paste. Alternatively, the flowable electrode may be a powder. This combination of features makes it possible to prepare electrochemical cells having very high anode-to-cathode interfacial surface area and relatively low separator volume. In fact, the principles of this invention can be employed to achieve a substantial increase in anode-to-cathode interfacial area and, therefore, a substantial improvement in discharge efficiency at high discharge rates, as compared with conventional cylindrical alkaline cells having a bobbin type cell construction wherein an anode is disposed within a cylindrical volume centrally formed in a cathode disposed adjacent an inner wall of a steel can defining the electrochemical cell, while maintaining, or even increasing, total cell capacity The first electrode includes a coating on surfaces of the first electrode, wherein the coating functions as a separator The separator coating is a thin film or layer of mateπal which is formed on the surface of the electrode The coating is at least initially secured to the surface of the electrode by mechanical, chemical or electrical forces After the cell has been assembled, the coating may no longer remain secured to the electrode surface In contrast, conventional separator mateπals are carefully converted into a dry free-standing film pπor to placing the separator adjacent the surface of an electrode Conventional separators conform to the surface of the electrode on a macroscopic scale and thus are not capable of forming uniformly thick layers on the surface of an irregularly shaped electrode Separator coatings are also distinguished from conventional separator mateπals by the fact that separator coatings are initially bound to the electrode surface along the entire interfacial area between the separator and electrode It is not necessary for the separator material to remain bound to the electrode after the cell has been assembled Examples of suitable separator coatings include coatings formed by apply g a polymeric coatmg composition to the electrode or electrode mateπal and converting the polymeπc coatmg composition into a polymer film Such polymeric coating compositions can be prepared by dissolving a polymer, such as cellulose, in a solvent Suitable separator coatings can also be formed by polymerising the separator coating directly on surfaces of an electrode A more detailed description of various separator coatings suitable for use with the invention are set forth in US Serial No 09/410,300 filed 30 September 30, the entire content of which is incorporated herein by reference Preferably, the separator coatings or films used in this invention have a thickness of about 100 micrometres or less, and more preferably a thickness of less than 60 micrometres, even more preferably less than 40 micrometres, and most preferably less than 30 micrometres Because of the substantial reduction m thickness of the separator coatings used herein, as compared with conventional paper separators (typically having a thickness of at least 200 micrometres), it is possible to substantially increase the anode-to-cathode interfacial surface area while reducing total separator volume Accordingly, the use of separator coatings having a thickness of less than 100 micrometres, less than 60 micrometres, less than 40 micrometres, or less than 30 micrometres, will allow production of electrochemical cells simultaneously exhibiting improved discharge efficiency at high discharge rates, and increased total discharge capacity For example, a separator coating having a thickness of 25 micrometres would facilitate production of a AA-size electrochemical cell having about 10 times the anode-to-cathode interfacial surface area of a conventional AA-size battery design using a bobbin type configuration with a 250 micrometre separator, without decreasing total capacity Alternatively, the thinner separator coatings can be used to make electrochemical cells having a combination of increased anode-to-cathode interfacial surface area, improved discharge efficiency at high discharge rates, and higher total capacity In addition to facilitating the production of thinner separators, the use of a separator coating formed directly on the surface of an electrode makes it practical to construct electrochemical cells with electrodes having highly irregular shapes and a high surface area This is in contrast to conventional paper and cellophane separators which can, in general, only conform with planar and smoothly curved electrode surfaces More specifically, the inability to conform conventional paper and cellophane separators to irregular surfaces has limited their use to electrochemical cells having plate electrodes, πbbon electrodes and cylmdπcally shaped electrodes An attempt to conform conventional paper or cellophane separators to an irregularly shaped electrode will generally cause the separator to become folded upon itself and occupy an unacceptably high portion of the volume of an electrochemical cell, whereas the separator coatings used in this invention can be formed directly on irregularly shaped surfaces of an electrode to achieve a substantially uniformly thin separator which does not occupy an unacceptably large volume m an electrochemical cell Another important feature of this invention is the use of a flowable second electrode mateπal which is capable of flowing around and surrounding the surfaces of an irregularly shaped, non-symmetncally shaped and/or non-cy ndπcally shaped separator coated first electrode An example of an electrode having a non-symmetπcal and a non-cyhndπcal shape is a spirally wound electrode or a dendπtic zinc electrode (which is descπbed later herein) The use of a separator coated electrode in combination with a flowable second electrode mateπal provides an economical way for producing electrochemical cells having a very high anode-to-cathode interfacial surface area and, therefore, an improved discharge efficiency at high discharge rates, without sacπficmg total discharge capacity In an embodiment that uses a spirally wound πbbon electrode, for example an electrochemical cell construction as shown m Figure 1 , the cell may be constructed by depositing a flowable electrode mateπal into a can or housing, and then inserting a spirally wound, separator coated electrode into the can As the spirally wound electrode is inserted into the can, the flowable electrode material flows upwardly filling the spaces defined by the spirally wound electrode and preferably completely surrounds the surfaces of the spirally wound electrode Alternatively, the cell may be made by first inserting the spirally wound electrode into the can, and thereafter depositing electrode matenal into the can so that it flows around and between the surfaces of the spirally wound electrode and the can Electrically conductive leads may be attached to the upper end of the spirally wound electrode, either before or after the spirally wound electrode is inserted into the can The electrochemical cell may be completed in a conventional manner with a seal and a cover Preferably, the second electrode mateπal constitutes a positn e electrode and the first electrode is a negative electrode In this case, the first electrode preferably compπses zinc as anode material, preferably m the form of a ribbon such as zinc foil, and the second electrode mateπal preferably includes manganese dioxide as cathode active mateπal Alternatively, the second electrode is the negative electrode, in which case the flowable mateπal co npπses anode active mateπal A flowable mateπal compπsmg zmc as anode active mateπal can be compnsed of, for example, a mixture of zinc, a binder, potassium hydroxide, water, and optionally, a gelling agent Other suitable electrode mateπals may be chosen according to the desired battery type and cell chemistry For example, the first electrode or second electrode mateπal may includes at least one electrochemically active mateπal selected from lithium, nickel, metal hydπde, cadmium, carbon, graphite, and thiated manganese dioxide An advantage of the present invention, particularly in an embodiment that uses a spirally wound πbbon electrode, for example an electrochemical cell construction as shown m Figure 1, is that it eliminates various problems associated with conventional methods of manufactuπng spirally wound or jelly-roll electrochemical cells Spirally wound electrochemical cells are conventionally produced by winding an anode and cathode together with a first separator disposed between the anode and the cathode In a conventional process the separator and electrodes must be properly aligned before winding of the electrodes and separator By forming a separator directly on at least one of the electrodes, in accordance with the present invention, the need for aligning the separator with the electrodes is eliminated, and the need for aligning a first electrode with a second electrode is eliminated This simplifies battery assembly, and, thereby, reduces the cost of fabπcating a spirally wound battery Equipment for winding a single web is less expensive than equipment for simultaneously winding and aligning three or more webs The anode is generally a metal foil, and the cathode is generally a composite material compπsed of a particulate electrode material and a binder In order to allow spiral winding of the cathode with the anode, the binder must be flexible Additionally, conventional machines for winding a cathode and anode together are more expensive than machines used for winding a foil anode alone Accordingly, the present invention allows an electrochemical cell construction, for example as shown in Figure 1, that eliminates the need for expensive jelly-roll winding machines and eliminates the need for a flexible binder in the cathode mateπal Thus, cell constructions are enabled that allow spirally wound electrochemical cells to be produced less expensively Additionally, the separator coatings on each side of the spirally wound πbbon electrode can be thinner and occupy less volume than conventional paper or cellophane separators, thereby facilitating production of spirally wound electrochemical cells having higher anode-to-cathode interfacial surface area and/or increased total capacity In an alternative embodiment, the cell includes a πbbon electrode having a separator coating and folded in a zigzag fashion, for example an electrochemical cell construction as shown in Figure 2 The folded electrode is inserted into the can and is surrounded by a flowable electrode mateπal The electrode material may be deposited into the can before or after the separator coated electrode is inserted into the can In further alternative embodiments, the first electrode may compπse a porous fixed network of an electrochemically active mateπal, such as zinc, or a porous fixed network of an electπcally conductive material, such as brass, on which is deposited an electrochemically active material, such as zmc Examples, such as metal foams and "dendπtic zmc" are descπbed below Thus, in one embodiment, the electrochemical cell compπses a separator coated porous metal (such as zinc) electrode inserted in the can, for example an electrochemical cell construction as shown in Figure 3 The porous or reticulated electrode can be a metal foam or sintered metal electrode Metal foams may be produced by a variety of known methods For example, a molten metal may be placed under high pressure so that it dissolves a non-reactive gas When the pressure is released and the metal is allow ed to cool, the dissolved gas escapes and leaves open-celled pores in the metal body In another process, foaming agents may be added to molten metal Another process mixes monomers with metal particles and heats the mixture to induce foaming and solidification of the resin In another process metal particles can be compressed in a conventional manner under suitable conditions of elevated temperature and pressure to form an anode having a desired shape The temperature and pressure employed are not particularly cπtical provided complete sintering and coalescence of the particles does not occur. Temperatures at approximately the sintering temperature of the metal at the pressures employed are preferred. Alternatively, the metal particles can be dry mixed with a powdered resinous binder such as polytetrafluoroethylene. The admixture of metal particles and binder may be compressed in a conventional manner, again under suitable conditions of elevated temperature and pressure to form an anode having the desired shape. The temperature depends upon the resin selected and the pressure applied which is normally at from about 1.7 to 170 MPa (250 to 25,000 pounds per square inch). Another method of fabricating an electrode having an open-pore structure involves depositing a metal by arc vapour deposition on and in an openwork synthetic- resin pyrolyzable support by juxtaposing the support with a pair of electrodes at least one of which is composed of at least one element of the selected metal. The electrodes are advanced into contact to strike an electric arc between the electrodes and evaporate the metal from one of the electrodes and effect deposition of the metal on the support. The space in which the support is juxtaposed with the electrodes is evacuated prior to or during deposition of the metal, whereby a fraction of a total amount of the metal adapted to ultimately form the open-pore structure is deposited in the form of a coating. In a spray-deposition operation, a quantity of the metal sufficient to make up the remainder of the total amount is sprayed onto the support and/or the coating. Thereafter, the support is pyrolyzed to form an openwork skeleton consisting essentially of the metal. In a final step, the metal skeleton is sintered into a coherent body constituting an open- pore structure. Further details of this method are set forth in US-A-5, 01 1 ,638. The reticulated or porous metal electrode (e.g., metal foam, sintered metal, etc.) may be provided with a separator coating by any suitable method, for example using any of the techniques set forth in US Serial No. 09/410,300 filed 30 September 1999. Thereafter, the separator coated porous electrode is inserted into the can and surrounded by flowable electrode material which flows around and into the pores of porous the electrode. Alternatively, the porous electrode may be inserted into the can before being provided with the separator coating The flowable mateπal may be added to the can before and/or after the porous electrode has been inserted In accordance with another embodiment, for example as shown in Figure 4, the electrochemical cell includes a three-dimensional tree-like structure of a metal, such as a mateπal known as "dendπtic zinc", which resembles the veins of a leaf, and which is coated with the separator coating The electrode which has the separator coating is immersed in a can containing the flowable cathode mateπal, for example a slurry of a cathode mix Alternatively, the flowable mateπal is added after the electrode has been inserted Suitable methods for prepaπng dendπtic zinc electrodes are disclosed in US- A-3,071,638 and US-A-3,753,779 which are incorporated herein In a preferred embodiment of the first aspect, a battery is provided that compπses a housing having an inteπor wall, a first electrode disposed in the housing, the first electrode coated with a separator material, and a flowable mixture of a second electrode material and an electrolyte dispensed in the housing such that the flowable mixture flows around the coated first electrode and between the first electrode and the interior wall of the housing According to this preferred embodiment, preferably the first electrode includes at least one strip including an electrically active material, preferably a zmc ribbon The stπp may, for example, be spirally wound or folded in a zigzag pattern Alternatively, the first electrode may comprise a porous fixed network of an electrochemically active mateπal such as zmc, or may comprise a porous fixed network of an electrically conductive mateπal on which is deposited an electrochemically active mateπal such as zmc The battery may comprise one first electrode or a plurality of first electrodes, each coated with a separator mateπal, and each disposed into the housing such that the flowable mixture flows around the coated first electrodes and between the first electrodes and the inteπor wall of the housing Preferred is that the second electrode material constitutes a positive electrode and the first electrode a negative electrode. For example, the second electrode material may include manganese dioxide, and the first electrode preferably includes zinc. However, alternatively one of the first electrode and second electrode material may include lithium, nickel, metal hydride, cadmium, carbon, graphite and or lithiated manganese dioxide. In another preferred embodiment of the first aspect, a battery is provided that comprises: a housing; a formed negative electrode disposed in the housing, the formed negative electrode including zinc, and the formed negative electrode coated with a separator; and a flowable mixture of an electrolyte and a positive electrode including manganese dioxide dispensed within the housing such that the flowable mixture surrounds the negative electrode. In a preferred embodiment of the second aspect, a method of making a battery is provided that comprises the steps of: dispensing a flowable electrode material in a housing; forming an electrode having a fixed structure; coating the electrode having a fixed structure with a separator material; and immersing the coated electrode in the flowable electrode material within the housing. The present invention will be further understood by reference to the embodiments shown in the drawings, in which: Figure 1 is an exploded perspective view of a spirally wound electrochemical cell in accordance with the invention; Figure 2 is a schematic cross-sectional view of an electrochemical cell having a ribbon electrode folded in a zigzag pattern in accordance with the invention; Figure 3 is a schematic longitudinal cross-sectional view of an electrochemical cell having a porous metal electrode in accordance with the invention; and Figure 4 is a schematic longitudinal cross-sectional view of an electrochemical cell including an electrode having a three-dimensional fractal structure in accordance with the invention Thus, an embodiment of the invention is shown in Figure 1 In accordance with this embodiment, an electrochemical cell 10 is constructed by depositing a flowable electrode mateπal 12 into a can or housing 14 and inserting a spirally wound, separator coated electrode 16 into can 14 As spirally wound electrode 16 is inserted into can 14, flowable electrode mateπal 12 flows upwardly filling spaces 18 defined by spirally wound electrode 16 and completely surrounds the surfaces of spirally wound electrode 16. As an alternative, electrochemical cell 10 can be made by first inserting the spirally wound electrode 16 into can 14, and thereafter depositing electrode material 12 into can 14 so that it flows around and between the surfaces of electrode 16 and can 14 Electπcally conductive leads 20 may be attached to the upper end of spirally wound electrode 16 either before or after spirally wound electrode 16 is inserted into can 14 Electrochemical cell 10 is completed in a conventional manner with a seal 22 and a cover 24 An alternati e embodiment of the inv ention is shown in Figure 2 In accordance with this embodiment, an electrochemical cell 30 includes a ribbon electrode 32 having a separator coating 33 folded in a zigzag fashion Folded electrode 32 is inserted into can 34 and is surrounded by a flowable electrode material 36 Electrode material 36 may be deposited into can 34 before or after separator coated electrode 32 is inserted A further alternative embodiment of the invention is shown in Figure 3 In accordance with this embodiment, an electrochemical cell 40 comprises a separator coated porous metal (such as zinc) electrode 42 inserted in can 44 Porous or reticulated electrode 42 can be a metal foam or sintered metal electrode The reticulated or porous metal electrode is provided w ith a separator coating Thereafter, separator coated porous electrode 42 is inserted into can 44 and surrounded by flowable electrode material 46 which flows around and into the pores 48 of porous electrode 42. A further alternative embodiment of the invention is shown in Figure 4. In accordance with this embodiment, an electrochemical cell 50 includes a three- dimensional tree-like structure 52 of a metal, such as a material known as "dendritic zinc", which resembles the veins of a leaf, and which is coated with a separator. The electrode 52 which has a separator coating 53 is immersed in a can 54 containing a slurry of cathode mix 56. Many modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that, within the scope of the appended claims, the invention may be practised otherwise than as specifically described.

Claims: CLAIMS: 1 A battery compnsing a housing, a first electrode disposed in the housing, a coatmg which functions as a separator, the coatmg located on a surface of the first electrode, and a flowable second electrode mateπal, the flowable second electrode mateπal disposed in the housing and surrounding the coated surface of the first electrode 2 A battery according to claim 1, wherein the first electrode has a non-cyhndπcal shape 3 A battery according to claim 2, wherein the first electrode has a non-symmetrical shape 4 A battery according to claim 1, wherein the first electrode comprises a ribbon electrode 5 A battery according to claim 4, wherein the ribbon electrode is spirally wound 6 A battery according to claim 4, wherein the ribbon electrode is folded in a zigzag pattern 7 A battery according to claim 4, wherein the ribbon electrode is comprised of a 8 A battery according to any preceding claim, in which the separator coating has a thickness of less than 100 micrometres, preferably less than 60 micrometres, more preferably less than 40 micrometres, most preferably less than 30 micrometres 9. A battery according to claim 1 , wherein the first electrode is a porous metal electrode 10 A battery according to claim 9, wherein the porous metal electrode is a metal foam 11 A battery according to claim 9, wherein the porous metal electrode is a sintered metal 12 A battery according to claim 9, wherein the porous metal electrode is compπsed 13 A battery according to claim 9, wherein the first electrode compπses a porous fixed network of an electrochemically active matenal 14 A battery according to claim 9, wherein the first electrode comprises a porous fixed network of an electrically conductive material on which is deposited an electrochemically active material 15 A battery according to claim 13 or claim 14, wherein the electrochemically active mateπal is zmc 16 A battery according to any preceding claim, wherein the second electrode material constitutes a positive electrode and the first electrode is a negative electrode 17 A battery according to claim 16, wherein the second electrode material includes manganese dioxide 18 A battery according to claim 16, wherein the first electrode includes zinc 19 A battery according to claim 1, wherein one of the first electrode or second electrode mateπal includes at least one electrochemically active mateπal selected from the group consisting of lithium, nickel, metal hydπde, cadmium, carbon, graphite, and lithiated manganese dioxide 20 A method of making a battery compnsing providing a housing, providing a first electrode, forming on a surface of the first electrode a coating which functions as a separator, disposing the coated first electrode in the housing, and disposing a flowable mateπal in the housing, the flowable material including a second electrode mateπal, the flowable material surrounding the separator coated on the surface of the first electrode 21 A method according to claim 20, wherein the first electrode comprises a ribbon electrode 22 A method according to claim 21 , wherein the πbbon electrode is spirally wound 23 A method according to claim 21, wherein the πbbon electrode is folded in a zigzag pattern 24 A method according to claim 21 , wherein the ribbon electrode is comprised of a 25 A method according to claim 20, in which the separator coating has a thickness of less than 100 micrometres, preferably less than 60 micrometres, more preferably less than 40 micrometres, most preferably less than 30 micrometres 26. A method according to claim 20, in which the first electrode is disposed into the housing before the flowable material is disposed into the housing. 27. A method according to claim 20, in which the flowable material is disposed into the housing before the first electrode is disposed into the housing. 28. A method according to claim 20, wherein the first electrode is a porous metal electrode. 29. A method according to claim 28, wherein the porous metal electrode is a metal foam. 30. A method according to claim 28, wherein the porous metal electrode is a sintered metal. 31. A method according to claim 28, wherein the porous metal electrode is comprised of zinc.

Inventors: AYERS ALAN D, AYERS KATHERINE E, BAILEY JOHN C, HUGHES PAULA J, SCHUBERT MARK A, TANG NGHIA C, VANDAYBURG MARK D, WHITE NEAL CHARLES, AYERS, ALAN, D., AYERS, KATHERINE, E., BAILEY, JOHN, C., HUGHES, PAULA, J., SCHUBERT, MARK, A., TANG, NGHIA, C., VANDAYBURG, MARK, D., WHITE, NEAL, CHARLES
Applicants: EVEREADY BATTERY INC, EVEREADY BATTERY COMPANY, INC.
Application year: 2000
Main classification: H01M
IPC codes: H01M2, H01M4, H01M6, H01M10