Patent Application
20070092794
The present invention generally relates to electrochemical battery cells. More particularly, the invention relates to electrochemical battery cells, such as alkaline cells, having balanced power and energy delivery capability for high to mid-range power levels of discharge through moderated surface area interface configurations between electrode components.
The present invention also relates to nickel oxy-hydroxide (NiOOH) formulation and its application in electrochemical battery cells. More particularly, the invention relates to a particular formulation of NiOOH, and related method of formulation, as well as its use in electrochemical battery cells, and more particularly those embodiments described herein.
Alkaline batteries based on manganese dioxide cathodes and zinc anodes are widely used for consumer portable electronic applications. There is a large market for primary alkaline cells in standard cylindrical formats such as AAA, AA, C, and D sizes. These products have numerous advantages. Zinc and manganese dioxide are inexpensive, safe, and environmentally benign and the system provides good energy density. For the consumer, these standard alkaline products have long offered a simple and convenient universal solution for an array of electronic products.
There has been a proliferation in recent years, however, of new portable electronic devices including personal digital assistants, MP3 recorders and players, DVD players, digital cameras, or the like. There is also a trend toward smaller and lighter portable electronic devices that limit the onboard battery size. Compared to earlier devices, such as, for example, transistor radios, the power consumption for many of these new devices can require higher continuous or pulse currents. Conventional or even premium alkaline cell designs cannot efficiently deliver their stored energy at the higher drain rates.
These inefficiencies under high rate discharge are related to internal resistance and electrochemical limitations of the conventional alkaline bobbin-cell construction. While much effort has gone into improving the energy content of the conventional alkaline bobbin cell by optimizing the internal packing and ionic conductivity of the electrodes, the fundamental design itself has changed little.
As shown in
The can 12 is closed at the bottom, and it has a central circular pip 22 serving as the positive terminal. The upper end of the can 12 is hermetically sealed by a cell closure assembly which comprises a negative cap 24 formed by a thin metal sheet, a current collector nail 26 attached to the negative cap 24 and penetrating deeply into the anode gel to provide electrical contact with the anode, and a plastic top 28 electrically insulating the negative cap 24 from the can 12 and separating gas spaces formed beyond the cathode and anode structures, respectively. The material of separator 20 may consist of laminated or composite materials or combinations thereof. Typically separator materials comprise an absorbent fibrous sheet material wettable by the electrolyte, and an insulating material being impermeable to small particles but retaining ionic permeability.
While the bobbin cell construction is a simple design that allows for high-speed, low-cost manufacturing, the surface area between the anode and cathode in a conventional bobbin cell is limited to the geometrical surface area of the cylinder of separator between the anode and cathode. Thus, for a bobbin cell, the anode to cathode interfacial surface area (Si) constituted by the interposed straight cylinder of separator is necessarily a fraction of the external surface area (Se) formed by the cylindrical wall of the can [(Si)/(Se)<1].
In the field of batteries, the surface area of—and between—the electrodes of an electrochemical cell is understood to be an important design element, since the mass transport flux of ions between anode and cathode (typically slower than electron transfer or chemical kinetics) can be a rate limiting or current limiting physical process. It is not only the ionic conductivity and surface area between the anode and cathode that is important but also the micro-porosity and surface area inside the electrodes.
It is possible to arrange for greater electrode and interfacial area within a cylindrical cell. The most widely used cylindrical cell design alternative to the bobbin cell is the spirally wound or jelly-roll construction which is well described in the Handbook of Batteries [3rd Edition, editors D. Linden and T. B. Reddy, Section 3.2.11, McGraw-Hill, 2002]. In this construction thin strips of anode and cathode with separator between them are tightly wound together. The electrodes can be as thin as a few tenths of a millimeter and for the spirally wound cylindrical cell the anode to cathode interfacial surface area can be several multiples of the external surface area formed by the cylindrical wall of the can [(Si)/(Se)>>1]. The greater interfacial area comes at the expense of additional complexity and cost to manufacture. Spiral winding requires precision alignment of anode, cathode, and separator, with lower production rates and higher capital equipment costs than “bobbin” construction cells. The spirally wound design is not typically applied to the alkaline MnO2/Zn cell where it would defeat the economic advantage of the materials, but is applied to more premium electrochemical systems including rechargeable nickel cadmium (NiCd) and nickel metal hydride (NiMH) batteries, and non-rechargeable systems such as lithium iron disulfide (LiFeS2) batteries.
Another trade-off of the spiral wound design is the higher amount of separator and current collector required, which take up volume that could otherwise be utilized for active material. Since a standard size cylindrical cell has a fixed volume, it is most efficiently built with maximum active material and electrolyte in order to maximize its energy content. In the bobbin cell, in addition to lower separator content and thick electrodes, the brass nail anode current collector and cathode current collection via contact with the cylindrical container wall do not significantly intrude on the interior space.
Thus, while converting from a bobbin design to spiral wound design increases the inter-electrode surface area and power capability, it also reduces the energy content of the cell. A spiral wound construction may deliver most of its energy efficiently for discharge rates on the order of 20 C(C refers to a current equivalent to the rated capacity of the cell in ampere-hours divided by 1 hour). Such high rate discharge capability may be essential for applications such as power tools, however is not typically needed for consumer electronics. Even devices such as digital cameras typically operate at more moderate discharge rates on the order of ⅓ to 1 C rate.
More costly spirally wound batteries may be over designed for many portable applications. However, for alkaline manganese dioxide cells with a zinc anode and potassium hydroxide electrolyte to maintain their competitive advantage as a universal solution for a wide range of consumer applications, better run time at higher drain rates is needed. Much of the recent patent literature related to the alkaline cell is aimed at addressing this issue.
In addition to material and electrode formulation strategies to improve power capability, there have been a number of strategies to increase the interfacial surface area between the anode and cathode through modifications of the conventional bobbin cell. For example, Urry in U.S. Pat. No. 5,948,561 describes the use of a bisecting conductive plate coated with cathode active material to partition a V-folded tubular separator. Luo et al. in U.S. Pat. No. 6,261,717 and Treger et al. in U.S. Pat. No. 6,514,637 also describe the creation of multiple anode cavities that are in these cases molded into the cathode pellets. Getz in U.S. Pat. No. 6,326,102 describes a relatively more complex assembly with two separate zinc anode structures in contact with the inner and outer contours of separator encased cathode pellets. Jurca in U.S. Pat. No. 6,074,781 and Shelekhin et al. in U.S. Pat. No. 6,482,543 describe stepped interior or contoured interior surfaces of the cathode pellet. Shelekhin et al. in U.S. Pat. No. 6,482,543, Lee et al in U.S. Pat. No. 6,472,099 and Luo et al. in U.S. Pat. No. 6,410,187 describe branched or lobed interior electrode structures.
All of these design strategies have limitations in the effective increase in surface area that is possible and introduce additional complexities that detract from the utilitarian design of the conventional bobbin cell. Some may achieve greater surface area but at the sacrifice of a cell balance change that decreases the energy content. Multi-cavity or multiple electrode designs introduce the need for more complex current collection and end seals. The more complex geometries may introduce orientation requirements and the need for more complex tooling and machinery for assembly. Complex geometries can make it difficult to apply separator uniformly and consistently especially in high-speed production, and may necessitate unconventional approaches such as internally applied conformal coatings.
For example, branched or lobed designs have limited ability to increase surface area unless the lobes are made thinner which makes applying separator and filling uniformly with gelled anode more difficult. If the lobes or branches are not thinner and longer then not much increase in surface is provided and the cell balance may be changed to be less efficient due to changes in relative cross-sectional area of the anode and cathode structures. Alignment of cathode pellets and breakage of pellets in lobed designs could make manufacture difficult.
The foregoing problems associated with typical bobbin and spirally wound electrode configurations are not limited to cylindrical cell configurations. Thinner product profiles and more efficient use of battery compartment space are also driving a trend toward the use of thin prismatic (rectangular) cell formats and free-form cell formats. Analogs to the bobbin and spirally wound cell constructions also exist for prismatic cells, such as, for example, those shown in the Handbook of Batteries, [3rd Edition, editors D. Linden and T. B. Reddy, Section 3.2.11, McGraw-Hill, 2002]. In the simplest designs of prismatic cells, opposed unitary anode and cathode masses exchange ions across an interposed separator boundary. As an example, U.S. Patent Application Publication No. 2003/0157403 (Shelekin et al.) describes a thin prismatic IEC 7/5 F6 size alkaline cell with unitary opposed electrode masses in which the total interfacial area between the anode and cathode is less than the projected cross sectional area of the cell. Thus, such designs do not address the aforementioned power characteristic problems.
There are two design alternatives to increase power in a prismatic cell configuration. The wound cell construction can be adapted by winding the strips of electrodes on a flattened mandrel that may then be compressed before placing in the cell container. Alternatively, surface area within a prismatic cell can be increased by an assembly of alternating anode/cathode stacked electrode plates, with like electrodes connected in parallel within the cell. Both of these methods, however, are more complex and costly to produce than a simple bobbin cell.
In the case of prismatic cells, additional design considerations related to internal pressure arise. Alkaline cell products must remain within maximum allowable dimensions under all anticipated conditions of use and at all states of charge. These products do incorporate a safety vent but under a broad range of normal use conditions they are effectively sealed. Alkaline cell container walls must therefore be sufficiently constructed to contain any internal pressure caused by any gas generation or expansion associated with the cell's electrochemistry. Design accommodations can include low gassing zinc formulations and free internal volume for expansion, wherein the balance of the design relies on the mechanical strength of the container.
A cylindrical container is an effective pressure vessel with uniformly distributed hoop stresses acting to reduce radial strains and the wall thickness of cylindrical alkaline cells may be as little as 0.008″. However, the prismatic form is not as effective at accommodating internal pressure and non-uniform bulging may occur with maximum deflections at the midpoint of the long wall spans. While increasing the wall thickness of the container can prevent bulging of the container, this also reduces the internal volume available for active electrode masses.
Having described many of the shortcomings of the prior art, the present invention is intended to, among other things, address these as well as other shortcomings in the prior art.
A battery cell such as a cylindrical or prismatic alkaline cell exhibiting significantly improved capacity utilization at mid-range power levels of discharge and maintaining much of the energy content and other feature advantages of typical cylindrical or prismatic alkaline cells by implementing a cell construction that produces increased surface area between the anode and cathode. In accordance with the principles of the present invention as embodied and described herein, one particular characterization of the present invention comprises an electrochemical battery cell comprising a cell housing defining an interior space having an interior surface, a first terminal and a second terminal. The cell further comprises an inner electrode encapsulated by a separator and disposed within the interior space of the housing. The inner electrode is in a curvilinear-like configuration and is formed such that an outer extent of the inner electrode is generally conforming to a contour defined by the interior surface of the cell housing. The inner electrode is in electrical communication with the second terminal of the housing. An outer electrode is disposed within the interior space of the housing such that it is in ionic communication with the inner electrode and in electrical communication with the first terminal of the cell housing.
Another embodiment of the present invention is directed to a battery cell, such as a cylindrical or prismatic alkaline cell, exhibiting significantly improved capacity utilization at high discharge rates while maintaining much of the energy content and other feature advantages of typical cylindrical or prismatic alkaline cells, by implementing a cell construction that produces increased surface area between the anode and cathode. In accordance with the principles of the present invention as embodied and described herein, one particular characterization of the present invention comprises an electrochemical battery cell comprising a cell housing defining an interior space having an interior surface, a first terminal and a second terminal. The cell further comprises an inner electrode encapsulated by a separator and disposed within the interior space of the housing. The inner electrode is in a folded configuration and is formed such that an outer extent of the inner electrode is generally conforming to a contour defined by the interior surface of a portion of the outer electrode. The inner electrode is in electrical communication with the second terminal of the housing. A portion of the outer electrode is disposed within the interior space of the housing such that it is in ionic communication with the inner electrode and in electrical communication with a first portion of the outer electrode that is in contact with the first terminal of the cell housing.
According to one particular aspect of the present invention, the inner electrode is in a curvilinear-like geometric configuration; the interior surface of the housing is in electrical communication with the first terminal and electrical communication between the outer electrode and the first terminal is established by contact between the outer electrode and the interior surface of the housing; and the inner electrode is an anode and the outer electrode is a cathode, wherein the first terminal has a positive polarity and the second terminal has a negative polarity.
According to another aspect, the inner and outer electrodes interface with each other to define an inter-electrode surface area (Si) and the cell housing further includes an exterior surface defining an exterior surface area (Se). The ratio of the inter-electrode surface area to the external surface area of the housing of the battery cell (Si/Se) is in the range of about 2 to about 8.
According to another aspect, an electrochemical battery cell comprises a cell housing defining an interior space, a first terminal and a second terminal; and an electrode assembly disposed within the interior space of the housing. The electrode assembly comprises an inner electrode encapsulated by a separator and having a folded configuration, and an outer electrode having a folded configuration intermeshing with the folded configuration of the inner electrode. The electrode assembly is formed such that an outer extent of the electrode assembly is generally conforming to a contour defined by the interior surface of the cell housing. The inner electrode is in electrical communication with the second terminal of the housing and the outer electrode is in electrical communication with the first terminal of the housing.
According to yet another aspect, an electrochemical battery cell comprises a cylindrically-shaped cell housing defining an interior space, a first terminal and a second terminal. The cell further comprises an electrode assembly disposed within the interior space of the housing. The electrode assembly comprises a pair of outer electrodes and an inner electrode encapsulated by a separator and disposed between the outer electrodes. The electrode assembly has a folded configuration such that each of the electrodes intermeshingly engages the other. The electrode assembly is formed such that an outer extent of the electrode assembly is generally conforming to the cylindrically-shaped cell housing. The inner electrode is in electrical communication with the second terminal of the housing and the outer electrode is in electrical communication with the first terminal of the housing.
According to yet another aspect, an electrochemical battery cell comprises a cell housing defining an interior space, a first terminal and a second terminal. The cell further comprises an inner electrode having a linearly geometric configuration having a cross-sectional area substantially less than an exterior surface area of the inner electrode and disposed within the interior space of the housing. The inner electrode is encapsulated by a separator and in electrical communication with the second terminal of the housing. The cell further comprises an outer electrode material disposed and formed within the interior space of the housing such that the inner electrode is embedded therein. The outer electrode is in ionic communication with the inner electrode and electrical communication with the first terminal of the cell housing.
According to yet another aspect, an electrochemical battery cell comprises a cell housing defining an interior space, a first terminal and a second terminal. The cell further comprises an electrode assembly disposed within the interior space of the housing. The electrode assembly comprises an inner electrode encapsulated by a separator and an outer electrode. The electrodes are intermeshed together to form an interface and compressed such that an outer extent of the electrode assembly is generally conforming to a contour defined by the interior surface of the cell housing. The inner electrode is in electrical communication with the second terminal of the housing and the outer electrode is in electrical communication with the first terminal of the housing.
Methods of manufacturing an electrochemical battery cell in accordance with the principles of the present invention are also contemplated. According to a particular aspect of the present invention, a method of manufacturing an electrochemical battery cell is provided comprising the steps of: providing a battery cell housing including an interior space, a first terminal and a second terminal; providing an inner electrode having a substantially flat configuration and encapsulated by a separator; providing an outer electrode having a substantially flat configuration; disposing the outer electrode adjacent the inner electrode; folding the inner and outer electrodes together into a folded configuration; forming the inner electrode such that an outer extent of the electrodes is generally conforming to a contour defined by the interior space of the cell housing; and disposing the electrodes within the interior space of the housing such that the outer electrode is in electrical communication with the first terminal of the cell housing and the inner electrode is in electrical communication with the second terminal of the cell housing.
Another method of assembly of the inner electrode and electrode sub-assembly of an alkaline cell includes forming a planar electrode into a curvilinear-like geometry. The planar electrode is grasped by a hollow mandrel and rotated into the desired form having at least one spaced region. The folded inner electrode can then be placed inside the ring of an outer electrode material in the cell container wherein an inner cathode material can then be introduced into an at least one spaced region via injection through the hollow mandrel or through some other nozzle placed in the at least one spaced region and withdrawn as the cathode material fills in; or, prior to inserting the folded inner electrode within the cell housing, elongated masses of inner electrode material can be inserted into the at least one space region wherein the inner electrode and elongated masses of inner electrode material are compressed into a single electrode sub-assembly and then placed within the ring of the outer electrode material of the cell container.
Other methods in accordance with the principles of the present invention are contemplated as well.
The methods of manufacturing an electrochemical battery cell in accordance with the principles of the present invention can be readily translated to automated high-speed production. One or more steps of these methods can be envisioned as replacing certain unit operations in a conventional bobbin cell manufacturing plant, with others being similar to those for conventional bobbin manufacturing, while maintaining equivalent throughputrates.
In addition a novel formulation of nickel oxy-hydroxide (NiOOH) is proposed in view of an associated method of formulating the NiOOH compound for use with an electrochemical battery cell. Cells made with the novel NiOOH formulation were found to provide increased energy capacity greater than known NiOOH cells produced under conventional methods. The formulation is derived from oxidation of nickel hydroxide using sodium hypochlorite solution without the presence of an alkaline hydroxide (e.g., lithium, sodium or potassium hydroxide). Without the presence of the alkaline hydroxide environment, the NiOOH material has been found to have superior performance when utilized in an electrochemical battery cell.
When utilized in a particular battery cell configuration as described herein, the above-described NiOOH formulation provides both increased response to energy demands and is of relatively low cost. Also the NiOOH electrodes made according to the present invention are more easily manufactured. This particular electrochemical battery cell has a simple and low cost construction with power and energy capacities comparable to more complex and more costly battery cell constructions.
These and other aspects of the present invention will be apparent after consideration of the written description, drawings and claims herein.
FIGS. 29A-C is a schematic diagram depicting aspects of a method of manufacturing and a related embodiment in accordance with the principles of the present invention.
FIGS. 30A-C is a schematic diagram depicting aspects of a method of manufacturing and a related embodiment in accordance with the principles of the present invention.
While the present invention is capable of embodiment in many different forms, there is shown in the drawings, and will herein be described in detail, one or more specific embodiments with the understanding that the present disclosure is to be considered an exemplification of the principles of the invention and is not intended to limit the invention to these specific embodiments.
The present invention also provides a simple and effective design of a battery cell, such as a cylindrical cell, with balanced energy and power characteristics intermediate between the bobbin and spiral wound designs and which retains the advantages of both designs, i.e., low cost, simple manufacturing with higher power, and high internal volume utilization for energy efficiency. In an embodiment, this is achieved by providing a significant but balanced increase of anode to cathode interfacial surface area in conjunction with thinner, high ionic conductivity, electrode structures. The present invention also provides a better balanced alkaline “modified” bobbin design which can be applied to various cell sizes including AAA, AA, C, D and others, so that higher capacity is available at higher drain rates while the favorable energy storage characteristics are retained.
An exemplification of this higher capacity benefit of the present invention is shown in
An effective way to characterize the ability of the invention to provide a well-balanced ratio of power to energy is to perform certain tests on assembled cells. The particular test utilized consists of a series of discharge steps to evaluate performance at a high rate discharge followed by a lower rate discharge to evaluate total capacity delivery capability. The specifics of the test for a AA size cell are: (1) a continuous discharge at 1.0 A to a voltage cutoff of 1.0 V; (2) a 30 second open circuit test; (3) a continuous discharge at 1.0 A to a 0.8 V cutoff; (4) a 30 minute open circuit test; and, (5) a 3.9 Ohm discharge to 0.7 V cutoff. This test is identified by the assignee of the present invention as a DCC4STP2 test. Other size cells may be tested similarly, but with increased or reduced current levels to reflect the capability of the cell size.
By performing tests of this type on cells utilizing the current invention and on conventional bobbin-type alkaline cells, a clear distinction in performance can be established. A capacity delivery ratio (CR) can be calculated by dividing the capacity delivered to 1.0 V at 1.0 A (C1V) to the total capacity delivered (CT) in the test. Because the present invention utilizes an effective linearly geometric and thin inner electrode (thin meaning having a cross-sectional area substantially less than an exterior surface area of the inner electrode), the capacity ratio (CR) will be significantly higher than that achieved in conventional bobbin-type alkaline cells.
Having demonstrated some of the performance benefits over conventional cells, the apparatus of battery cells in accordance with the principles of the present invention will now be described. Referring now to the drawings, in which like numerals refer to the like parts throughout the several figures,
Referring to
Since the inner electrode 32 is a porous solid structure, the elements 32B can be thinner and longer than lobes or branches of prior art designs. For example, in a AA cell, the inner electrode 32 may be extruded into a shape that has thin elements 32B only 0.040-0.080 inches thick, whereas the equivalent anode diameter in a conventional AA alkaline cell would be about 0.30 inches. In this case, the inner electrode 32 can be accessed from each side of the element 32B with the maximum effective diffusion thickness equal to one half the through thickness. By using a solid inner electrode, not only can thinner geometric elements be achieved—by virtue of not needing to fill a narrow void with gel as with prior designs—but the conformal coated separator 34 can be applied to an external surface 37 of the inner electrode 32 by dipping or spraying—rather than attempting to apply a separator to the inner surface of a complex geometry outer electrode as with prior designs. The outer electrode 36 can then be applied around the separator encased inner electrode 32, either external to the cell housing 31 or after the inner electrode is disposed within the cell housing 31. In an embodiment wherein the outer electrode is applied within the housing 30, the inner electrode 32, in the form of an anode and having a linearly geometric configuration, can be inserted into the housing 31 which can then filled with a cathode powder and pressed to form an embedded inner electrode 32.
Another way of achieving the embedding of the inner and outer electrodes in the cell housing would be to bend or fold the electrodes together externally to the housing to form an electrode geometry, mold the electrodes into a shape or contour conforming to the housing, and then inserting them together into the housing. Referring now to
As shown in
In an alternate embodiment as shown in
The present invention facilitates an increase in anode to cathode interfacial surface area such that the ratio of inter-electrode surface area (Si) to external surface area of the cell container or housing (Se), i.e., (Si)/(Se), may be in the range of 2 to 8 for a AAA or AA cell, (or possibly higher for larger diameter cell sizes like C or D) in order to markedly enhance high rate discharge characteristics. The increased interfacial area provides for a cell design with internal resistance that is a fraction of that of a bobbin cell constructed of equivalent materials. In the examples set forth herein below, the impedance measured at 1 KHz was 70% or less of that of a conventional bobbin cell. Power and energy content are better balanced so that the present invention retains greater than 70-80% of the energy content of a conventional bobbin at moderate rate while increasing the utilization at high power.
A particular embodiment of the present invention provides an inner electrode that has thinner average through thickness measure than the equivalent inner electrode in a conventional bobbin cell. By thinning the inner electrode through-thickness the surface area can be increased significantly by lengthening the cross dimension so that approximately the same optimal anode to cathode cell balance can be maintained. The decreased through-thickness dimension of the inner electrode provides shorter diffusion lengths, which further enhances power capability of the cell. A conventional alkaline AA size bobbin cell has a cathode ring wall thickness of approximately 0.1 to 0.15 inches and an anode core thickness of approximately 0.2 to 0.3 inches, whereas an alkaline AA cell in accordance with the principles of the present invention may have a cathode thickness of approximately 0.035 to 0.070 inches and an anode thickness of only 0.020 to 0.060 inches.
Another benefit of the present invention is the increased utilization of the inner electrode at high discharge rates. A conventional bobbin cell has a low utilization at high rates because of the internal cylindrical geometry. As the discharge of the anode proceeds radially inwards from the inner surface of the separator, the anode to cathode interfacial surface area is constantly decreasing. This effectively increases the current density at the discharging inner electrode surface and leads to shutdown of the discharge reaction due to transport limitations. Increasing the surface area and thinning the inner electrode maintain a more uniform current density throughout the discharge leading to increased utilization of the inner electrode material.
In a preferred embodiment, the longitudinal dimensions of the inner and outer electrodes are approximately equal to the full internal height of the container minus the height required for the seal, which is typically at least 70% of the internal height so that the electrode composite occupies nearly the full length of the container and maximizes energy content. The outer electrode is preferably formed to be in direct contact with the interior surface of the housing and current collection from this outer electrode is principally via contact with and through the metal housing. The inner electrode is encased in separator and then embedded in an outer electrode matrix material, or sandwiched or formed with the inner electrode, wherein an insulated lead is brought out and then inserted into the housing so that the outer electrode contacts the inner surface of the housing.
In the case of an alkaline MnO2/Zinc cell, to which many of the exemplifications herein refer, the zinc anode is the inner electrode and the MnO2 cathode is the outer electrode which makes contact with the interior surface of the housing for a positive polarity contact. Note that while many examples herein consider the alkaline cell specifically, it is understood that the principles of the present invention can be applied to other electro-chemistries and formats.
According to a particular embodiment of the present invention, an alkaline manganese dioxide-zinc cell is provided comprising a manganese dioxide cathode, a zinc anode, a separator between the anode and cathode, and an aqueous alkaline potassium hydroxide electrolyte. The anode has a non-circular cross section with a short diffusion length relative to a conventional bobbin design anode such that the capacity of the active material is more distributed throughout the interior of the cross-section and cumulative cross-sectional perimeter which is more than twice the cell housing diameter. The anode is wrapped in separator and embedded in the cathode matrix which fills the space between the anode and the interior surface of the housing uniformly. The cell has a well-balanced ratio of power to energy and gets good capacity utilization at high discharge rate. In the case of a AA cell, this is exemplified by achieving greater than 1.2 Ah on a 1 Amp to 1 Volt discharge test.
In one embodiment, the present invention provides a cell comprising a substantially planar or substantially flat separator encapsulated zinc anode and one or two planar shaped cathodes that are formed into an accordion fold shape and then the whole cathode/anode assembly molded to fill the container.
The cathode structures are formulated such that they have the necessary physical integrity and electronic conductivity to permit handling in high speed production as well as to provide good electron transfer characteristics from the interior of the folds to the cell container wall. This can be accomplished by formulating the composite cathode with conductive fillers, reinforcing materials, binders or carrier webs. A particular means of achieving the necessary mechanical and electronic properties may be to apply a metal foil or mesh to the outer face of the cathode mass such that this metal structure provides an electronic contact to the interior surface of the housing and a continuous electrical connection to the interior of the folds.
Methods of manufacturing an electrochemical battery cell in accordance with the principles of the present invention are also contemplated, as should be apparent from the foregoing description. According to a particular aspect of the present invention, a method of manufacturing an electrochemical battery cell is provided comprising the steps of: (A) providing a battery cell housing including an interior space, a first terminal and a second terminal; (B) providing an inner electrode having a thin and substantially flat configuration and encapsulated by a separator; (C) providing an outer electrode having a thin and substantially flat configuration; (D) disposing the outer electrode adjacent the inner electrode; (E) folding the inner and outer electrodes together into a folded configuration; (F) forming the inner electrode such that an outer extent of the electrodes is generally conforming to a contour defined by the interior space of the cell housing; and (G) disposing the electrodes within the interior space of the housing such that the outer electrode is in electrical communication with the first terminal of the cell housing and the inner electrode is in electrical communication with the second terminal of the cell housing.
According to another particular aspect of the present invention, a method of manufacturing an electrochemical battery cell in the case of forming the outer electrode within the housing is also contemplated. The method comprises the steps of: (A) providing a battery cell housing including an interior space, a first terminal and a second terminal; (B) providing an inner electrode having a thin cross section in a linearly geometric configuration and encapsulated by a separator; (C) disposing the inner electrode within the interior space of the housing such that it is in electrical communication with the second terminal of the cell is housing; (D) disposing an outer electrode material within the interior space of the cell housing such that the inner electrode is embedded therein and is in electrical communication with the first terminal of the housing; and (E) pressing the outer electrode material disposed within the interior space of the cell housing.
Other methods and variations of these particular methods are contemplated and are considered within the scope of the present invention when understood by one of ordinary skill in the art after consideration of the descriptions herein.
In a particular embodiment in accordance with the principles of the present invention, a simple method of manufacturing is provided by which a preferred embodiment is achieved. According to a particular embodiment, two cathodes are formed onto die punched metal substrates and placed adjacent to a centrally placed separator encased anode structure. Thus positioned, the electrodes are intermingled and shaped by shaping dies applied perpendicular to the long axis of the electrodes. The final die is a concentric clamshell that forms the outer extent of the electrodes to conform to a contour or shape of the cell housing, such as a cylinder. After forming, the die opens slightly to allow the cylindrically formed integrated electrodes to be pushed into a cell housing positioned adjacent to the forming die. After the electrode assembly is in the housing, additional KOH electrolyte may be added to the top of the open housing for absorption into the electrodes as it passes to the next operation in sequence. The partially assembled cell at this stage has an approximately centrally placed insulated anode lead wire protruding from the top of the housing. This lead is passed through the center of a plastic bottom seal, and welded to an interior surface of a bottom cover, which is then oriented into its proper placement on the seal. Cell closing and finishing operations are equivalent to a conventional bobbin cell process.
The steps that form the improved cell design of the present invention can be readily translated to automated high-speed production. This formation sequence can be envisioned as replacing certain unit operations in a conventional bobbin cell manufacturing plant, with one or more of the steps being similar to those for conventional bobbin manufacturing. Cathode and gelled zinc anode mixing processes for example are expected to be reasonably similar as for conventional bobbin making. Certain of the modified bobbin assembly process operations may even be carried out with altered forms of the basic process equipment now used, with equivalent throughput rates.
To demonstrate and exemplify the principles of the present invention, several examples will now be given. The following examples apply to a general purpose MnO2/Zn AA cell that can provide greater runtime in a digital camera application, that is, the cell can deliver more capacity on a 1 Amp to 1 Volt discharge compared to a conventional MnO2/Zn AA cell. In addition the energy content of the cell is not excessively compromised such that reasonable capacity is still available at a moderate rate (3.9 ohm) discharge. Example cells were tested with a 1 Amp discharge to 0.8 Volt, recording the capacity achieved when the cell potential reaches 1 Volt, thereby simulating the ANSI digital camera test. After a 30 minute rest, there is an additional discharge step at 3.9 ohms to 0.7 volts. The 1 Amp to 1 Volt capacity (C1V), total capacity delivered (CT), and capacity ratio (CR) tabulated below, are indications of the high rate and low rate capacity utilization efficiency. The data in Table 1 relates to the specific examples presented and shows that the invention increases utilization on the digital camera test while not affecting utilization on low rate tests, demonstrating the benefit of the present invention over the prior art.
The examples refer to AA cells in Ni-coated steel cans of standard dimensions. The cathode formulation may be of any type that is typical of primary alkaline cells consisting of EMD (γ-MnO2), conductive powder, and the remainder being other additives such as binders and electrolyte. The electrolyte is an aqueous alkaline solution of usually 4N to 12N potassium hydroxide. The electrolyte may contain dissolved zinc oxide, ZnO, surfactants and other additives, so as to reduce the gassing of the active zinc within the negative electrode.
The MnO2 cathode premix formulation used in Examples I-VI consisted of a premix of Kerr-McGee High Drain EMD 69.4%, Acetylene Black 5.2%, KS-15 Graphite 2.6%, PTFE-30 Suspension 0.4%, and 9 N KOH 22.4%, on a weight basis. Mixing was carried out in a Readco mixer, ball mill, or other suitable mixer. The cathode premix was further mixed in the ratio of 100 g of mix to 1 g PTFE-30 suspension and 10 g of 9 N KOH solution in order to improve the pasting characteristics and for adhesion to the Ni substrate. The standard substrate was non-annealed expanded metal (Dexmet 3 Ni5-077). Seven grams of the cathode formula was pressed onto the substrate in a Carver press to give a cathode assembly thickness of about 0.047 inches. There was some loss of electrolyte (approx. 0.5-1.0 g) on pressing.
This is an example of the “embedded corrugated-fold” design as shown in
This example illustrates the “embedded corrugated-fold” design shown in
This example illustrates the “embedded corrugated-fold” design shown in
This example illustrates the “embedded corrugated-fold” design shown in
Other manifestations of the “embedded corrugated-fold” design of the present invention are anticipated. For example the assembly and process variables such as: anode weight, anode soak time, degree of compression, cathode formulation, cathode substrate, and cathode-to-can current collection can be “fine tuned” to maximize electrical performance of the embedded “W” design. Almost all of the cells were built with the 0.515 inch diameter compression die which was adapted over the previous standard 0.5 inch diameter die based largely on the clear observation that less electrolyte is squeezed out during assembly. It is important to retain enough electrolyte in the cell to facilitate performance.
It is also possible to vary the length of the electrodes or length and number of folds to provide more optimal surface area and filling of the container, than given in the W-fold described in the examples. Rather than using two outer cathode assemblies, a single length of cathode may be wrapped around the separator-encased anode and then folded into a corrugated structure. An alternate means to increase surface area is for multiple layers of cathode and anode to be used in the stack to be corrugated, for example: cathode/anode/cathode/anode/cathode.
Based on the description above, it should be understood by one of ordinary skill in the art that the principles of the present invention may be embodied in any type of cell configuration, including prismatic or free-form cell configurations. Nevertheless, for purposes of further exemplification, several prismatic cell embodiments will now be described in more detail.
Referring generally now to
The inner and outer electrodes 100 and 102 can be constructed in many different shapes depending on the particular application. Preferably, the inner and outer electrodes 100 and 102 are constructed in a substantially flat configuration having a rectilinear periphery. The electrodes 100 and 102 can then be formed together to fit within and conform to a particular cell housing (sometimes referred to herein as a can), such as a prismatic cell housing.
Referring to
Referring now to
Referring to
Referring to
Several examples of a prismatic cell construction in accordance with the present invention will now be described, which illustrate some of the performance characteristics of such cell construction. The examples apply to a general purpose MnO2/Zn cell in an IEC 7/5 F6 prismatic size (6 mm×17 mm×67 mm, 0.33 mm wall thickness, internal dimensions of approximately 15.74 mm×63.80 mm×4.95 mm) that can deliver high capacity on a 0.5 to 2 Amp discharge. In addition the energy content of the cell is not excessively compromised such that reasonable capacity is still available at a low to moderate rate discharge. Example cells were tested and the data shows that the invention increases utilization at higher discharge rates while not substantially affecting utilization on low rate tests.
The MnO2 cathode formulation used in the examples consisted of a premix of Kerr-McGee High Drain EMD 72.6%, KS-15 Graphite 8.2%, PTFE-30 Suspension 0.4%, and 9 N KOH 18.8%, on a weight basis. The cathode structures are formulated such that they have the necessary physical integrity and electronic conductivity to permit handling in high speed production as well as to provide good electron transfer characteristics from the interior of the folds to the cell container wall. This can be accomplished by formulating the composite cathode with conductive fillers, reinforcing materials, binders or carrier webs. A particular means of achieving the necessary mechanical and electronic properties may be to apply a metal foil or mesh to the outer face of the cathode mass such that this metal structure provides an electronic contact to the container wall and a continuous electrical connection to the interior of the folds. Mixing was carried out in a Readco mixer, ball mill, or other suitable mixer to provide suitable pasting characteristics for adhesion to the Ni substrate. The standard substrate was non-annealed expanded metal (Dexmet 3 Ni5-077).
In the following examples, zinc gel was utilized to form the anode assembly of the cells.
In Examples 5-8, the longitudinal dimensions of the inner and outer electrodes are approximately equal to the full internal height of the container minus the height required for the seal, which is typically at least 70% of the internal height so that the electrode composite occupies nearly the full length of the container and maximizes energy content. For the prismatic cell, the cathode weight was approximately 11 g and thickness about 0.041 inches. There was some loss of electrolyte (approx. 0.5-1.0 g) on pressing.
A test cell utilizing an electrode assembly of the present invention was fabricated and tested. The zinc gel comprised powdered metallic zinc or zinc alloys and optionally zinc oxide together with a suitable gelling agent such as carboxymethyl cellulose, polyacrylic acid, starches, and their derivatives. A separator pouch of approx. 28 mm×62 mm prepared out of Scimat SM700/79 separator containing a tin coated steel substrate was filled with approximately 5 g of zinc gel formulation consisting of 65% zinc powder, 34.5% KOH and 0.5% carbopol to form the anode assembly. A planar MnO2 cathode coated onto an expanded metal substrate of 60 mm×62 mm was wrapped around the anode using the fold configuration shown in
A second test cell utilizing an electrode assembly of the present invention was fabricated and tested. The zinc gel comprised powdered metallic zinc or zinc alloys and optionally zinc oxide together with a suitable gelling agent such as carboxymethyl cellulose, polyacrylic acid, starches, and their derivatives. A separator pouch of approx. 28 mm×62 mm prepared out of Scimat SM700/79 separator containing a tin coated steel substrate was filled with approximately 5 g of zinc gel formulation consisting of 65% zinc powder, 34.5% KOH and 0.5% Carbopol to form the anode assembly. A planar MnO2 cathode coated onto an expanded metal substrate of 60 mm×62 mm was wrapped around the anode using the fold configuration shown in
A third test cell utilizing an electrode assembly of the present invention was fabricated and tested. The zinc gel comprised powdered metallic zinc or zinc alloys and optionally zinc oxide together with a suitable gelling agent such as carboxymethyl cellulose, polyacrylic acid, starches, and their derivatives. A separator pouch of approx. 28 mm×62 mm prepared out of Scimat SM700/79 separator containing a tin coated steel substrate was filled with approximately 4.5 g of zinc gel formulation consisting of 65% zinc powder, 34.5% KOH and 0.5% Carbopol to form the anode assembly. A planar MnO2 cathode coated onto an expanded metal substrate of 60 mm×62 mm was wrapped around the anode using the fold configuration shown in
A fourth test cell utilizing an electrode assembly of the present invention was fabricated and tested. The zinc gel comprised powdered metallic zinc or zinc alloys and optionally zinc oxide together with a suitable gelling agent such as carboxymethyl cellulose, polyacrylic acid, starches, and their derivatives. A separator pouch of approx. 28 mm×62 mm prepared out of Scimat SM700/79 separator containing a tin coated steel substrate was filled with approximately 4.5 g of zinc gel formulation consisting of 65% zinc powder, 34.5% KOH and 0.5% Carbopol to form the anode assembly. A planar MnO2 cathode coated onto an expanded metal substrate of 60 mm×62 mm was wrapped around the anode using the fold configuration shown in
The discharge voltage curves for the four example cells are illustrated in
Other manifestations of the design of the present invention are anticipated. For example, the assembly and process variables such as: anode weight, anode soak time, degree of compression, cathode formulation, cathode substrate, and cathode-to-can current collection can be “fine tuned” to maximize electrical performance of the embedded “U” design. It is also possible to vary the length of the electrodes or length and number of folds to provide more optimal surface area and filling of the container, than given in the folded cells described in the examples.
As should be apparent to one of ordinary skill in the art from the foregoing description, the principles of the present invention can be applied in many different embodiments and implemented through many different methods of manufacturing and assembly. To further exemplify these principles and their broad scope of application, additional methods of manufacturing and embodiments of cells conducive to these methods will now be described.
As previously described herein, one particular embodiment of a cell of the present invention utilizes a planar electrode stack that is folded into a corrugated structure (or other folded configuration) and is then formed or molded to fit the cell container or housing. This type of embodiment has been shown to increase the anode to cathode interfacial surface area and provides increased power relative to a simple bobbin cell known in the art. Although methods of manufacturing cells of this type have been previously described herein, embodiments having this type of structure can be formed by other methods as well, which may be more cost effective and more conducive to manufacturability.
Methods that utilize a granulated form of outer electrode material, such as a cathode material formulation, have been shown to be more cost effective and more conducive to manufacturability. Various methods of manufacturing of embodiments utilizing granulated forms of outer electrode material will now be described in more detail for purposes of further exemplification of such embodiments.
The outer electrode material formulation, such as a cathode formulation, is easily mixed in a granulated form and can be easily stored in such a state prior to further processing, such as being pressed into molded rings or pellets, either externally or internally to the cell container. By utilizing a granulated form of outer electrode material, any broken pellets or other material loss can be easily fed back to the mixing or granulation stage of processing for rework, thereby further reducing manufacturing costs. This is one significant advantage over the use of sheeted or substrate forms of outer electrodes, where scrap rates can be higher due to increased dimensional and mechanical integrity constraints associated with conventional outer electrode substrate structures.
Referring now to
Referring now to
In a variation of the method illustrated in
Although many consumer electronic applications such as digital cameras demand alkaline cells having a high-power discharge capacity, it may be preferable in some applications, e.g., clocks and radios, to utilize cells having increased levels of mid-range power discharge capacity. To increase the mid-rate discharge capacity of an alkaline cell, alternate conformations of electrode assemblies may be utilized in place of the densely corrugated, or W structure, of the inner electrode used in the high power cells discussed above. More specifically, the interfacial area between the inner and outer electrodes can be configured to increase the mid-rate discharge capacity over high-rate discharge capacity. Such mid-range power configurations incorporate reduced quantities of electrode current collector and separator used to construct the cell. The decrease of these materials reduces the cell's manufacturing cost and simultaneously increases the volume available within the cell for insertion of additional active material. Utilizing more active material in construction of the cell will increase the cell's energy content.
The trade off between increasing a cell's energy and reducing its power can be accomplished by appropriately decreasing the amount of surface area between the inner and outer electrode. Instead of using a densely corrugated structure for the inner electrode, e.g., W-shape, an alternate geometric configuration having a less dense configuration can be utilized; for example, curvilinear-like geometry such as c, n, o, s, u, v, w, and z shapes.
Embedding the curvilinear-like shaped inner electrode and outer electrode, i.e., electrode assembly, into the cell housing can be achieved using any of the methods shown above.
A comparison of the curvilinear-like shaped inner electrodes of the mid-range power conformations to the densely corrugated, i.e., W configuration, of the high power inner electrode will now be discussed with respect to a conventional bobbin cell—shown in
Referring to
Referring to
Referring to
Referring to
A comparison of the ratio of interfacial areas of each electrode assembly conformation shown in
As can be seen by the chart above, some of the curvilinear-like geometries—particularly the v and o configured inner electrodes—provide a significant reduction in the interfacial area as compared to the more densely w configured inner electrode. In addition to the decreased manufacturing costs associated with the decrease of inner electrode material, e.g., anode current collector and separator material being utilized, the curvilinear-like geometries of
Regardless of the inner electrode's shape, electron flow between the interior and exterior portions of the outer electrode may be enhanced by applying a thin porous conductive coating, e.g., carbon, on the exterior surface of the separator encasing the inner electrode, which traces a path toward the container wall.
To further demonstrate the principles and scope of the present invention pertaining to alkaline cells having increased capacity for mid-rate discharge applications, several exemplifications are provided below.
All of the following examples refer to an alkaline AA cell construction in which the outer electrode is a cathode containing manganese dioxide and the inner electrode is an anode containing zinc. The inner electrode defines a folded, curvilinear-like shape appropriate for the desired discharge capacity of the alkaline cell. The outer electrode is formed of two distinct portions, an exterior portion being a stack of annular rings in contact with a wall of a cell container and an interior portion being one or more elongated masses shaped into the folds, or spaced regions, defined by the folded inner electrode. Alternatively, the interior portion of the outer electrode may also be granulated cathode material injected within the spaced regions defined by the curvilinear-like shape of the inner electrode. The interior portion of the outer electrode is operably connected to the exterior ring portion of the outer electrode near the outer edges of the fold(s) and as such, the outer electrode masses are made contiguous. The outer electrode does not contain a metallic current collector.
Various formulations, weights, and dimensions may be used for both the exterior portion, e.g., ring, and interior portion of the outer electrode, e.g., cathode. These parameters define the apportionment of the potential discharge capacity and anode-to-cathode surface area contact of the exterior and interior portions. As such, the parameters can be adjusted to optimize the performance of the cell in view of its intended application, i.e., high-rate discharge capacity, mid-rate discharge capacity.
For the examples discussed below, the interior cathode formulation is 71.4% EMD, 6.6% graphite (Superior Graphite ABG1010), 21.6% KOH and 0.4% PTFE suspension. The inner electrode of the below examples is 6.5 g of a zinc gel consisting of approximately 64.5% zinc powder, 35% KOH solution and 0.5% of a gelling agent. The inner electrode is contained in a heat sealed double layer pouch of Scimat 700/78 and 31/08 separator materials. The pouch also encloses a perforated tin-coated steel foil current collector with an insulated copper lead. The insulated copper lead emerges from the pouch for connection to the negative end terminal of the cell. The width of the pouch is varied to accommodate folding into the various geometric conformations so as to fit into the interior of the rings and at the same time permit good contact between the interior and exterior portions of the outer electrode, which is essential for efficient discharge of the entire electrode.
One method of assembly of the alkaline cell includes pressing a mass of granulated cathode material into an annular die to form a ring pellet. Preferably, three to four pellets are inserted into the cell container to form the exterior portion of the cathode. A gel filled anode pouch is pre-folded into the desired configuration and dipped into 9 N KOH solution. The interior cathode material is compressed and shaped to form elongated masses of the desired weight and dimensions, which are placed in the loose folds of the anode pouch. The anode/interior-portion-cathode assembly is placed in a cylindrical compression die and pressed to form a cylinder, which corresponds closely to the inner dimensions of the cathode ring. Additional 9 N KOH electrolyte is added and the anode connection is welded to the negative terminal end cap and the cell is sealed.
Several examples of alkaline cells incorporating various curvilinear-like shaped inner electrodes are discussed below.
O-shaped Inner Electrode—the exterior cathode mass is comprised of four 1.5 g pellets with a 0.420″ internal diameter and 0.525″ outer diameter, pressed from an 89% EMD, 6% graphite (Superior Graphite ABG1010) and 5% KOH mixture. The anode pouch is approximately 41 mm high by 28 mm wide, formed into an open cylinder. The interior cathode mass is a single rod-shaped mass weighing approximately 6 g.
S-shaped Inner Electrode—the exterior cathode mass is comprised of four 1.7 g pellets with a 0.420″ internal diameter and 0.525″ outer diameter, pressed from an 89% EMD, 6% graphite (Superior Graphite ABG1010) and 5% KOH mixture. The anode pouch is approximately 41 mm high by 34 mm wide, formed into a rolled S shape. The interior cathode mass is two bars of semi-circular cross section with a total weight of approximately 4.4 g.
W-shaped Inner Electrode—the exterior cathode mass is comprised of four 1.5 g pellets with a 0.436″ internal diameter and 0.527″ outer diameter, pressed from an 87% EMD, 8% graphite (Superior Graphite ABG1010) and 5% KOH mixture. The anode pouch is approximately 41 mm high by 39 mm wide, formed into a rolled corrugated W shape. The interior cathode mass is three flattened bars of rectangular cross section with a total weight of approximately 4.35 g.
S-shaped Inner Electrode with Carbon Coated Pouch—the cell is the same as Example 10, but the anode pouch rather than being dipped in KOH is dipped into a slurry prepared from 5 g of ABG1010 graphite in 50 ml of 9N KOH during the assembly process for applying a carbon coating to the separator.
W-shaped Inner Electrode with Carbon Coated Pouch—the cell is the same as Example 11, but the anode pouch rather than being dipped in KOH is dipped into a slurry prepared from 5 g of ABG1010 graphite in 50 ml of 9N KOH during the assembly process for applying a carbon coating to the separator.
The alkaline cell examples were electrically tested under the following parameters: a 1 Amp discharge to 1.0 Volts, followed by a 2 second rest, then 1 Amp discharge to 0.8 Volts, followed by a 30 minute rest, then 3.9 ohm discharge to 0.8 Volts, 2 second rest, 3.9 ohm discharge to 0.7 Volts. This test provides a means of assessing both high-rate and medium rate discharge capacity. More details for the above alkaline cell examples are provided below in Table 2.
Referring to the S-shaped inner electrode and electrode sub-assembly, one method of assembly includes steps shown in
Alternately, prior to inserting the folded inner electrode 100 within the cell housing 104, elongated masses of inner electrode material 106 can be inserted into the more open gaps (see
It is to be understood that for many embodiments described herein utilizing granulated cathode material, a pasted anode arrangement is preferably utilized (which is essentially dry) to counter-balance the addition of electrolyte and the use of an extra-wet cathode material. Any swelling of the inner anode arrangement caused by the electrolyte will essentially further tighten up tolerances associated with the electrode assemblies and ensure good contact between the inner anode electrode and the outer electrode material, which benefits the performance characteristics of the cell.
In accordance other aspects of the invention, one preferred formulation of NiOOH was prepared with the following method, importantly in the absence of alkaline hydroxide:
The preferred cathode mix was derived by mixing 87 gms of the NiOOH as prepared in accordance with the preferred method above with 8 gms of graphite in a ball mill for 6 hours. Then 5 gms of 9 molar KOH electrolyte was added and the mixture ball milled for another 2 hrs. The resulting cathode mix was used to make cathode formations for electrochemical cells according to another aspect of the invention.
In a preferred embodiment of a cathode formation, the above-described cathode material was used to form a cathode to be used in high power delivery rate cells as described herein. It is intended, however, that the cathode material disclosed herein may be used in and with other cells and electrochemistries including use in conventional bobbin cells.
In a particular embodiment, a battery cell is provided with a nickel oxyhydroxide cathode (prepared as described above) in place of a standard EMD cathode as described herein. The NiOOH cathode was found to impart a higher conductivity and higher operating voltage to the cathode such that much greater run time was possible on certain high drain tests.
The test discharge consists of a 1.5 W, 2-second pulse followed by a 0.65 W pulse for 28 seconds repeated ten times over 5 minutes followed by a 55-minute off period. This entire sequence is repeated each hour until the cell voltage falls just below 1.05 Volts.
As indicated in
The NiOOH cathode material as prepared and described herein above was apportioned and formed in steel dies via hydraulic pressure so as to be densely packed into cylindrical rings (for the outer cathode portion) and semi-cylindrical bars (for the inner cathode portion). The cell container was a standard size AA can of nickel-coated steel. The interior of the can was coated with a thin graphite layer. Four cathode rings of approximately 1.5 g each with a height of 0.39 inches were inserted into the can.
The cathode material was also formed into bars that were approximately 0.79 inches long, 0.11 inches thick with a weight of 1.16 g.
A perforated brass substrate with an emergent insulated lead was sealed into a double layer pouch of a membrane separator with 6.5 g of zinc anode gel uniformly distributed throughout. A 1.6 inch by 1.65 inch pouch was formed into a loose S-shape and dipped into an electrolyte comprising a graphite slurry of 9N potassium hydroxide solution.
The two cathode bars were then disposed in folds of the S-shape. This electrode subassembly was then lightly compressed to form a cylindrical shape that could then be inserted into a hollow interior of the rings inside the can. The anode lead was connected to the negative terminal of the end cap which was then sealed in place to create the cell.
It is contemplated that, in addition to the battery cell constructions described herein, the nickel oxy-hydroxide formulation aspect of the invention as described herein will provide increased energy capacity in a variety of battery cell constructions including conventional bobbin cells.
While specific embodiments have been illustrated and described herein, numerous modifications may come to mind without significantly departing from the spirit of the invention, and the scope of protection is only limited by the scope of the accompanying Claims.
This application claims priority to Provisional Application 60/718,406 filed Sep. 19, 2005 and is a continuation-in-part of U.S. patent application Ser. No. 10/904,097, filed Oct. 22, 2004, which is a continuation-in-part of U.S. patent application Ser. No. 10/710,135, filed Jun. 21, 2004, which is a continuation-in-part of U.S. patent application Ser. No. 10/710,116, filed Jun. 18, 2004, which is a continuation-in-part of U.S. patent application Ser. No. 10/846,020, filed May 14, 2004, which claims priority to Provisional Application Ser. No. 60/499,545, filed on Sep. 2, 2003; Provisional Application Ser. No. 60/503,298, filed Sep. 16, 2003; and Provisional Application Ser. No. 60/513,167, filed Oct. 21, 2003, all of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60718406 | Sep 2005 | US | |
| 60499545 | Sep 2003 | US | |
| 60503298 | Sep 2003 | US | |
| 60513167 | Oct 2003 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10904097 | Oct 2004 | US |
| Child | 11524085 | Sep 2006 | US |
| Parent | 10710135 | Jun 2004 | US |
| Child | 10904097 | Oct 2004 | US |
| Parent | 10710116 | Jun 2004 | US |
| Child | 10710135 | Jun 2004 | US |
| Parent | 10846020 | May 2004 | US |
| Child | 10710116 | Jun 2004 | US |
