ZINC ELECTRODES FOR NICKEL-ZINC ACCUMULATORS

Abstract: A long-lived, nickel-zinc cell which is characterised by a zinc electrode having a copper grid and an active material comprising zinc-rich particles and entangled natural cellulose fibres with or without calcium oxide or hydroxide and with or without lead compounds, and otherwise substantially free of customary binder materials.

Description: Nickel-zinc electric storage battery cells This invention relates to Ni-Zn electric storage batteries and more particularly to zinc electrodes for such batteries. Zinc electrodes have heretofore customarily been made by homogeneously mixing zinc oxide powder with binder materials such as polystyrene, polytetrafluoroethylene, polyvinylidene fluoride, methylcellulose, carboxymethylcellulose, polyvinylalcohol or polyethylene oxide and applying the mix to a conducting/supporting gridwork. Small quantities of lead (i.e., as Pb, PbO or Pb.O) or copper powder have been added to the zinc oxide mix to promote better utilization of the zinc, and hence, improve the capacity of the electrode. Likewise, HgO has been added to raise the hydrogen overvoltage and reduce H2 gassing. In addition to the foregoing, calcium hydroxide or calcium oxide has been added to the zinc electrode to promote the formation of insoluble calcium zincate rather than soluble potassium zincate. Formation of calcium zincate increases battery cycle life by reducing the formation of zinc dendrites which can bridge the interelectrode gap and short out the cell. Though the calcium zincate reduces dendrite formation, at least one observer has reported its tendency toward cementation, and hence, reduced effectiveness, on cycling. The zinc electrodes are separated from the nickel (i.e., NiOOH) electrodes by microporous membranes or separators as a final protection against interplate dendrite growth and internal cell shorting. These separators (typically sausage casing and the like) resist current flow within the cell. The higher the resistance of the separators, the lower the power and the greater the internal heating. Excessive internal heating of the battery shortens the live thereof. Zinc electrodes have traditionally suffered from a problem known as "shape change'1 which results from an uneven deposition of the zinc on the electrode on succeeding charge and discharge cycles. As a result, more zinc tends to accumulate in the centre of the electrode where it becomes dense and nonreactive. The edges of the electrode, on the other hand, become depleted of zinc. The net result is a deformed electrode having a very small effective surface area available for reaction. Shape change commonly occurs in plates having uneven current distribution therethrough, and the condition is amplified as the surface area of the electrode increases. Practical batteries having both energy and power capabilities (e.g., for electric vehicle applications) require relatively large .2 area electrodes generally greater than about 25 in (161.29 cm2). Zinc electrodes made from customary binder materials have demonstrated relatively poor capacity and power retention upon cycling (i.e., charging and discharging), and often fall below a useful level, for many applications, after two few cycles. It has been observed that electrodes so made often show signs of segregation of the zinc, zinc oxide and binder especially toward;the end of their useful life. For example, visual inspection of zinc electrodes made from risen-type binders (e.g., polystyrene) has shown that the initial homogeneous distribution of zinc oxide and binder is lost as cycling proceeds and small islands of zinc, zinc oxide and binder begin to appear across the face of the electrode. Moreover, microscopic examination of the cycled electrodes -reveals that the resin-type binders tend to concentrate nearer the grid and the zinc nearer the surface of the electrode. This segregation of binder and active material tends to progressively passivate the electrode as cycling progresses. The water-soluble/K0H-insoluble type binders (e.g., cellulosic-type),on the other hand, tend to migrate due to electrolyte concentration and temperature variations. Such variations affect the solubility of these watersoluble binders in a cycling environment and appear to cause local dissolution and precipitation as the concentration of the electrolyte changes. Studies of these electrodes show the formation of thin films of the binder on the surface of the electrodes. Instability of such binders coupled with the aforesaid film- formation tends to shorten the lives of zinc electrodes made therefrom. Because of the reduced effectiveness of the zinc electrode to effeciently utilize its zinc content, workers in the field have traditionally provided approximately three times more zinc electrode capacity than nickel electrode capacity (e.g., 300 AH of zinc oxide per 100 AH Ni(0H)2. According to the present invention a Ni-Zn battery, has a zinc electrode which is substantially free of customary binder materials and whose active material is prevaded with an entanglement of stable, reinforcing and hydrophilic fibres. The zinc active material preferably includes insoluble-zincate-forming additives, and said stable, reinforcing, hydrophilic fibres irrigate the active material and reduce the tendency of the insoluble zincates toward cementation. The invention is hereinafter particularly described with reference to the accompanying drawings -in which: Figures 1-4 are curves showing the performance of Ni-Zn cells made in accordance with the present invention. The invention comprehends a zinc electrode for an alkaline, Ni-Zn battery comprising a substantially homogeneous mixture of zinc-rich (i.e., zinc, zinc hydroxide, zinc oxide and/or calcium zincate) particles and entangled natural cellulose fibres and otherwise substantially free of customary binder materials. By "natural cellulose fibres" is meant cellulose fibres substantially as they occur in nature's plant life and without dissolution and regeneration from solution. Zinc electrodes containing natural cellulose fibres have demonstrated superior capacity and power retention after prolonged cycling. The precise mechanism by which the natural cellulose fibre holds the zinc-rich particles together and maintains capacity and power levels for prolonged periods is not completely understood. It is believed that the entangling of the fibres, in paper fashion, mechanically retains and strengthens the active material while the fibres' hydrophilicity irrigates the active material with electrolyte. Scanning electron microscope studies of cycled zinc electrodes show zincrich crystals #dhering to the fibres. Whatever the mechanism, prolonged life at high capacity and power levels has been observed. In a preferred embodiment of the invention, the zinc electrode also includes calcium oxide or hydroxide particles. These particles are substituted for some of the excess zinc otherwise normally provided to ensure capacity, and serve to trap the reacted zinc in situ in the form of insoluble calcium zincate. No more calcium hydroxide need be added than will react with the zinc in the cell environment. About 0.25-1.5 moles of the calcium compound per mole of zinc oxide has been suggested. Any amount more than that serves only to consume valuable space otherwise available for more zinc. When coupled with the natural cellulose fibre, passivation due to calcium zincate cementation is avoided, and much lower zinc oxide to Ni(OH) ratios than normally employed are possible. The 2 preferred electrode also includes a small quantity (i.e., no more than about 4.0% by weight) of lead. The lead improves the turn around efficiency (i.e., watthours out/watt-hours in) primarily in the early cycles. Substantially Pb-free electrodes, on the other hand, have somewhat less turn around efficiency in their early cycles, but have demonstrated higher retained capacities in the last half of their cycle life. In one test, for example, a test cell containing only zinc oxide, Ca(OH)2 and'newsprint, but no lead, lost only 4 of its capacity between cycles 100 and 290 and generally showed a capacity retention curve flatter near the end of cycling than that shown in Figure 2 for Pb-containing electrodes. Still further, the preferred embodiment includes a copper grid. The copper grid provides more uniform current distribution across the face of the electrode and reduces the internal resistance of the battery, both of which seem to have an effect on reducing the rate of shape change. It is preferred to use relatively low resistance polyolefinic separators such as Celgard 2400 or 2500 with suitable wetting agents. This reduces the internal electrical resistance of the cells and permits better electrolyte circulation. In this latter regard, the zinc electrode of the present invention makes possible the use of such low resistance separators whose porosity and pore size would not otherwise alone be adequate to suppress interplate dendrite growth for a prolonged period.. The copper grid provides more uniform current distribution throughout the electrode than would a higher resistance grid. Likewise, the more porous separators result in more uniform electrolyte concentration within the cells as well as lower internal resistance, and consequently, less heat.development and increased power. This combination (i.e., grid and separator) coupled with trapping of the zinc as calcium zincate and irrigation thereof with the cellulose fibres is seen to work in concert to suppress the rate of liferobbing dendrite growth and shape change while the low internal resistance reduces heating and improves power. The electrolyte is aqueous KOH preferably in the l0%-28% range. As the KOH approaches 30% the zincate becomes soluble and the-effects of the Ca(OH)2 is lost. For long-lived, deep-cycling batteries about 20% KOH seems best, while for shallow cycling uses such as an automotive cranking battery about 25% seems best for cold cranking performance. Zinc electrodes made in accordance with the present invention may be made from zinc, zinc oxide, zinc hydroxide or calcium zincate particles (hereinafter referred to as zinc-rich particles). Preferably, the electrodes are. made by mixing zinc oxide with the cellulose fibres as an aqueous slurry or paste and applying the mix to the grid (e.g., expanded metal, screen, perforated sheet, etc.). Thereafter, the electrode is pressed, dried and re-pressed to a predetermined finished thickness. Plates so made with zinc oxide are said to be in the "unformed" state, and are converted to zinc in the battery during formation which is the initial charge given to the battery. Thereafter, the electrode cycles between zinc, in the charged state, to Zn(OH)2 or calcium zincate (if used) in the discharged state. The natural cellulose fibres of the present invention are substantially free of the customary binders used heretofore, and hence, their tendency to passivate the electrode in time. This-is not to say that small quantities of such binders might not be used with the cellulose, but not in such quantity as to reduce the effectiveness of the cellulose in irrigating the electrode and prolonging its useful life. Successful electrodes have been made with wood-based cellulose fibres in the form of water-digested or repulped paper. In this regard, relatively low grade papers such as newsprint containing about 5% alpha cellulose, 20% lignin and 30% hemicellulose have proven nearly as effective as high grade filter paper (i.e., Whatman t42) made from cotton fibres and containing 98% alpha cellulose. Success has been achieved with fibre loadings ranging from about 0.5% to about 10% by weight of the active material mix. The lower concentrations are more than adequate, and in fact, are preferred for the making of thinner plates. In making the zinc electrode, a swatch of paper of appropriate weight is cut from a convenient source (e.g., roll or sheet). The swatch is then preferably cut in half. One of the halves is then cut or diced into very small squares, and such that the fibres are minced to lengths less than the size of the openings in the grid. The diced half and the undiced half are then added to water in a blender and stirred until the paper is repulped and a slurry of the fibres is formed. The other ingredients (I.E., zinc oxide, Ca(0H)2, Pb30#, etc.) are then added to the blender and homogenized with the cellulose fibres. The slurry is then applied to the grid. Thick slurries may be pasted onto the grid as by a spatula or conventional grid pasting equipment (e.g., belt paster). Thin slurries are best applied to the grid using a conventional vacuum table technique. In either event, one half of the slurry is applied to one face of the grid, and the other half of the slurry applied to the other face of the grid. The smaller fibres from the dicing operation bridge-the openings in the grid and become entangled with the long uncut fibres which tend to tie longer fibres together. Specific examples and test results A number of cells have been tested. Essentially, these cells comprised a nickel electrode, an appropriate separator system, a KOH electrolyte and the particular zinc electrode being tested. The cells had -- an odd number of plates (i.e., electrodes) stacked such that there was one more negative electrode than positive, and such that both end electrodes were negative electrodes (i.e¯., zinc). The end electrodes had approximately one-half the capacity of the other negative electrodes in the centre of the cell stack-. All electrodes, both positive and negative, were 7.2 inches (18.288 cm) tall by 3.911 inches (10.0076 #cm) wide. The nickel electrodes were substantially the same for all tests and included a nickel plaque substrate (i.e., General Electric Co.) impregnated with nickel hydroxide and cobalt hydroxide. The plaque included a perforated steel sheet (i.e., 0.004 inch (.1016 mm) thick) nickel plated to a Ni thickness of about 0.00025 inch (.00635 mm) Ni. The perforations had a diameter of about 0.077 inch and a density of about 78 perforations per square inch of substrate. The sheet is then coated by the manufacturer with carbonyl nickel powder.-and sintered to form a substrate which is 0.036 inch (.9144 mm) thick, has an overall (i.e., including steeisheet) -pd-rosity of about 73% and an average pore size of about 10 microns. The plaque was impregnated by immersing it in a two-molar solution of Ni nitrate including about 5% cobalt nitrate and cathodically forming Ni(OH)2-in its pores. The cobalt or equivalent material, barium, is used to improve the charge efficiency of the electrodes. The completed electrodes comprised 24.7 gms of Ni(oHj2 and 1.3 gms of Co(OH)2 and had a theoretical capacity of about 7.52 ampere-hours (AH) each. Test cells were assembled in an essentially noncompressed fashion such that the separator and bibulous mats (where used) were lightly held between the plates. The plates were immersed in the electrolyte and "formed" to approximately 200% of the capacity (i.e., ampere-hours) of the nickel electrode. Thereafter, they were discharged at about the 3 hour rate (i.e., about 30 amps) to about (85% of the theoretical capacity (ampere-hour) of the nickel plate (i.e., to a cut-off voltage of about 1.0). Thereafter, the cells were recharged at about 9-12 amperes to a cut-off voltage of 2.25 volts or about 90% of the theoretical capacity of the nickel electrode (i.e., about 5% overcharge). This cycle was repeated and data collected during cycling. Figure 1 shows the retained capacities of substantially identical cells exept for their zinc electrodes. The curve shown by the dashed line had a polystyrene binder for the zinc electrode while the cell represented by the solid line contained no customary binder but rather only repulped newsprint in admixture with the other active material ingredients. This cell had 13 positive plates and 14 negative plates arranged as described above. The negative plates had a zincplated copper grid (i.e., expanded metal) and an active material comprising 37.2 grams of zinc oxide, 0.56 grams HgO and the binder. The cell represented by the dotted line had 2.23 grams of polystyrene as the binder for the zinc oxide while the cell represented by the solid line had 4.3 grams of repulped newsprint mixed with the zinc oxide. The zinc electrodes were made as described above. The polystyrene bound electrode used as emulsion of polystyrene identified as Richamer HME and supplied by the Richardson Co. The several plates were assembled into a 27-plate 74 ampere-hour (AH) cell. The negative plates were wrapped with two layers of Fibrous sausage casing (FSC) and the positive plates wrapped with two layers of polypropylene membrane, Celgard K-513. Celgard K-513 is essentially a laminate of Celgard 2400 (microporous polypropylene) and a nonwoven bibulous mat bonded to one side thereof and impregnated with appropriate wetting agents. The mat-side contacted the nickel plate. The data of Figure 1 shows that after five cycles both cells had the same capacity (i.e., about 74 ampere-hours) while at 100 cycles the cellulose zinc cell still had a capacity of 60 ampere-hours or about 81% of its original capacity, while the polystryene zinc cell had a capacity of only 41 ampere-hours or about 55% of its original capacity. These cells had a ZnO-to-Ni(OH)2 ampere-hour ratio of 3.26:1. Figure 2 shows the retained energy. and power capacity in terms of percent of original capacity of a particularly preferred embodiment of the invention. The test cells from which the Figure 2 data was derived comprised 29 plates including 14 positive and 15 negative plates and each had a theoretical nickel electrode capacity of 105 ampere-hours. The nickel plates were as described above whereas the central negative plates were as described hereafter The end negatives had half the capacity of the central negative plates. Each central zinc electrode (in the unformed condition) comprised 20.1 gms of zinc oxide, 13.8 gms Ca(OH)2, 1.35 gms Pb304 and 0.44 gms of newsprint. Some electrodes had a copper grid weighing about 5 gms and formed by punching a plurality of closely spaced onequarter inch diameter holes across the face of a thin copper sheet while other electrodes had expanded copper grids also weighing 5 gms. The averageparticle sizes for the ZnO, Ca(OH)2 and Pb3 04were abort 1.6 microns, 7.9 microns and 2.3 microns, respectively. About 0. 22 grams of the newsprint was diced into small squares less than one-quarter inch (6.35 mm) on each side to provide about 50% short cellulose fibres. The newsprint was added to about 400 millilitres of H20 in a Waring blender and repulped to a homogeneous slurry of cellulose fibres. Thereafter, the zinc oxide, Ca(OH)2 and Pb304 was added and blended into a homogeneous slurry and then cast onto the grid on a vacuum table as described above. The plates were then pressed dried and repressed to a finished thickness of about 0.038 inch (.8522 mm). The zinc and nickel plates were then each wrapped with a bibulous mat of unwoven nylon (i.e., ca. .005 inch ( .1275 cm) thick) which is 50-85% porous. Such materials as Pellon 2501, Cerex 3605, 3607 and 3610 have proven successful. Unwoven polypropylene mats such as Kendall 1583 or Kimberley Clark's S-95 or S-96 have also proved effective. The mat spaces the separator from the plate and permits better circulation of electrolyte in the plate-separator space. The mat-wrapped electrodes were then each wrapped in two layers of microporous polypropylene separator material (i.e., Celgard 2400). Celgard 2500 has also been used successfully. The lower resistance 2500 separators are preferred for their higher porosity (i.e., 45%) and larger pore size (i.e.,O.ll)O, and hence, lower internal resistance. The separators are folded over the bottom of the plates and heat sealed together along the sides thereof. These test cells had a theoretical capacity of about 105 ampere-hours, an actual working capacity (i.e., @ 85% depth of discharge) of about 89 ampere-hours and a ZnO:Ni(OH)2 ampere-hour ratio of 1.76. As can be seen from Figure 2, at 250 cycles the cell still retains about 80% of its original capacity (i.e., energy) and about 96% of its original power. The power was determined by periodically drawing 300 amps from the cell for about 30 secs at the beginning of a discharge cycle. At the end of about 300 cycles, the cell was subjected to several discharge rates (i.e., between recharges) and the cell voltage drop and output capacity determined for the several rates. Figure 3 shows how very little the cell's capacity varys with discharge rate. In this regard, at the 25 ampere rate that cell demonstrated a capacity s of 62.3 AH and at the 100 ampere-rate it demonstrated a capacity of 55AH. Similarly, Figure 4 shows how little the cell voltage falls off at very high discharge rates. Hence, even after over 300 cycles, the capacity of the preferred cells still demonstrated a surprising ability to deliver its energy even at very high rates. Still other tests have been made with a cell containing 33 plates and a separator system like that described in conjunction with the 29-plate cell of Figure 2. This cell had a theoretical capacity of about ll9AH derated to l0lAH at 85% of its theoretical capacity. The zinc electrodes have copper grids and an active material mix comprising 15.31 gms zinc oxide, 11.48 gms Ca(OH)2, 1.04 gms Pb304 and 0.37 gms of newsprint. This cell has a ZnO:Ni(OH)2 ampere-hour ratio of only 1.34 and after some 276 cycles has performed substantially the same as the above 29-plate test cell as shown in Figure 2. Still further reduction in the zinc oxide/Ni(0H)2 are expected as the basic 2 formula is optimized. As this ratio is reduced, the energy density of cells made therefrom increases.

Claims: Claims The embodiment of the invention in which an exclusive property or privilege is claimed are defined as follows: 1. An alkaline nickel-zinc electric storage battery cell having a nickel electrode and a zinc electrode spaced therefrom, and an aqueous alkaline electrolyte bridging the space between the electrodesp characterised in that said zinc electrode comprises a conductive grid embedded in a homogeneous mixture of zinc-rich particles and sufficient natural cellulose fibres to hold said particles in place on said grid, but otherwise essentially free of customary binder materials. 2. An alkaline nickel-zinc cell according to claim 1, characterised in that calcium oxide and/or hydroxide particles are included with said zinc-rich particles. 3. An alkaline nickel-zinc cell according to claim l or 2, characterised in that said electrolyte is a potassium hydroxide electrolyte and that said zinc electrode comprises a copper grid embedded in a homogeneous mixture of comminuted zinc oxide, calcium hydroxide Pb304 and natural cellulose fibres, the calcium hydroxide content being 0.25 to 1.5 moles of calcium hydroxide per mole of zinc oxide, the Pb304 content being up to 4% by weight of the mixture and the cellulose content being about 0.5% to about 10% by weight of the mixture 4. An alkaline nickel zinc cell according to any of claims 1 to 3, characterised in that at least a portion of said fibres is smaller than the openings in said grid.

Inventors: JONES, RICHARD ALAN
Applicants: GENERAL MOTORS CORPORATION
Application year: 1980
Main classification: H01M4
IPC codes: H01M4