US3905830A

US3905830A - Zinc fibers and needles and process for preparing the same

Info

Publication number: US3905830A
Application number: US231831A
Authority: US
Inventors: Demetrios V Louzos
Original assignee: Union Carbide Corp
Current assignee: Edgewell Personal Care Brands LLC
Priority date: 1970-04-03
Filing date: 1972-03-06
Publication date: 1975-09-16
Anticipated expiration: 1992-09-16

Abstract

Process for the preparation of stable, high surface area, virtually pure zinc filaments and in particular zinc fibers and needles having a unique crystal structure consisting essentially of one or more single crystals preferentially orientated with an ''''a'''' axis parallel to the axis of the filament. The zinc fibers and needles are prepared by the electrolysis of a soluble zinc salt-containing electrolyte solution under conditions of extremely high cathode current density.

Description

United States Patent Louzos Sept. 16, 1975 [5 ZINC FIBERS AND NEEDLES AND 2,820,077 1/1958 PROCESS FOR PREPARING THE SAME 397L638 1/1963 3,291,707 12/1966 [75] Inventor: Demetrios V. Louzos, Rocky River, 3,32 7 3 /19 7 Ohio [73] Assignee: Union Carbide Corporation, New Primary ExaminerJohn H. Mack York, NY. Assistant Examiner-C. F. LeFevour Filed: Man 1972 Attorney, Agent, or FirmJ. R. Doherty 121] App]. No.: 231,831

[57] ABSTRACT Related U.S. Application Data i621 Division of S 25490 Apn-l 3, 1970, Process for the preparation of stable, high surface abandoned area, virtually pure zinc filaments and in particular zinc fibers and needles having a unique crystal struc- 52 U.S. Cl. 136/31; 136/76; 204 12 wre Consisting essentially Of one or more Single y [51] Int. Cl. 11011:: 41/00 tals preferentially orientated with an axis Parallel [58] Field f Search 136/30, 31, 76, 125, to the axis of the filament. The zinc fibers and needles 204/10 14 12, 55 R are prepared by the electrolysis of a soluble zinc saltcontaining electrolyte solution under conditions of ex- 5 References Cited tremely high cathode current density.

UNITED STATES PATENTS 10 Claims, 12 Drawing Figures 2,655,472 10/1953 Hilliard et al 204/10 FIBER MA1\' PATENTED SEP I 6 I975 SM] l L]? 6 Fl BER MAT FIGJ PATENTEDSEFIEIBYS I I 3.905.830

SIEET ILUF ANODIC POLARIZATION CURVES AT -2oc ANODIC CURRENT VIN, AMPERES A ,Z 5 400 o I a I ZINC FIBER (j COMPACT z 2 o I o ZINC I '||m=|.02 A/In? :2 POWDER I g 3 (MC GEL I E 3 o L- lim= 2 j Alll't g z I 5 200 m' I m I Q I I o 400 2 I I u I z I N o 0.63 l.27 I-- APPARENT ANODIC CURRENT DENSITY m AMPERES/SQ. IN.

FIG. 4. A

PATENTED SEP I 6 I975 FIG.

FIG.

PATENTEDSEPIBISIS $805,830 $5121 a 0? 8 FIG. 9;

PATE'NTED SEP I 6 I975 seem 7 9? 8 0.0.0.0....XQIIOI.

POTENTIAL O zmc ANODE m 0.8 CELL VOLTAGE '3 O O I l I HOURS ZINC FIBERS AND NEEDLES AND PROCESS FOR PREPARING THE SAME This is a division of application Ser. No. 25,490 filed Apr. 3,1970, now abandoned.

This invention relates to zinc filaments in general and more particularly to novel zinc fibers and needles and to a process for their preparation. The zinc filaments can be used to fabricate anodes for both primary and secondary galvanic cells especially, though not exclusively, of the type using an alkaline electrolyte.

BACKGROUND OF THE INVENTION Galvanic cells of the type employing a zinc anode and an alkaline electrolyte generally requirethat the anode possess a high surface area. This requirement is essential for reducing the tendency of zinc to passivate in the alkaline environment and furthermore to obtain satisfactory high rate discharge, particularly at low temperatures, by a more efficient utilization of the active zinc material.

Prior art high surface area ainc anodes for use in alkaline galvanic cells have been made using conven' tional zinc powder. In one form of anode, the zinc powder is suspended within a suitable gelling agent such as carboxymethyl cellulose containing the alkaline electrolyte, these particular anodes being often referred to as gelled powder anodes.

The difficulty with anodes of this type is that the gelling agent, which is electrochemically inactive and thus capable of performing no useful purpose other than to support the zinc powder, takes up considerable space which might otherwise be occupied by the active material and consequently its use necessarily reduces the volumetric efficiency of the cell. Another serious problem is that the zinc powder from which these anodes are made usually contains substantial amounts of metallic impurities. These metallic impurities are capable of forming local cell couples with zinc which can give rise to wasteful corrosion of the anode and to the generation of gas during storage of the cell. These problems can be effectively overcome by amalgamating the zinc powder prior to fabricating the anode but this is an expensive procedure and increases the cost of manufacturing the cell.

In sealed secondary or rechargeable alkaline galvanic cells using a gelled powder anode, it has been furthermore found that the gelling agent is readily oxidized and tends to break down upon repeated cycling, thatis, charge and discharge, and thus destroys the mechanical integrity of the anode body. Another serious problem encountered with these gelled powder anodes is that under conditions of overcharge the gel network tends to prohibit rapid oxygen recombination with the active anode material and consequently dangerous internal gas pressures may devclopin the sealed cells.

High surface area anodes have also been fabricated from a dendritic zinc sponge produced by electrolytic methods such as disclosed in US. Pat. No. 3.07l,638 issued to M. B. Clark et al. on Jan. 1, 1963. While this dendritic zinc sponge is advantageous in that it can be produced substantially free of impurities, it possesses an extremely high surface area and is pyrophoric and susceptible to spontaneous combustion if proper care is not taken in handling the materialduring the fabrication of the anode.

SUMMARY OF THE INVENTION The invention contemplates the provision of novel zinc filaments and in particular novel zinc fibers and needles possessing certain properties which make them ideal for use in fabricating galvanic cell anodes. The zinc fibers and needles of the invention are quite readily distinguishable in physical appearance from other forms of zinc material heretofore known in the art. The zinc fibers of the invention may best be described as filaments having a thin elongated central spine portion with a number of poly-directional side growths or branches. The zinc needles of the invention may best be described as filaments having a fairly smooth central spine portion with only a few or a minimum of poly-directional side growths or branches. The term filament as used herein refers in the broadest sense to any thin elongated bodywhose length may be hundreds or thousands of-times greater than its width, and possessing considerable tensile strength, toughness and pliability. The term poly-directional as used herein refers to the physical arrangement of the side growths or branches which, during formation, tend to grow in many different directions or along many planes and is used specifically to denote the three dimensional character of the fibers and needles as distinguished from the flat fern-like structure of dendritic particles.

Thenovel zinc fibers and needles of the invention are primarily characterized by their stability, unique crystal structure, exceptional purity and high surface area. The zinc fibers and needles are stable in that they do not rapidly oxidize upon exposure to the atmosphere. The crystal structure of the zinc fibers and needles is unique and readily distinguishable from any other form of zinc material. Broadly, the zinc fibers and needles may be defined as being composed of one or more single crystals having a preferred orientation. More precisely, the zinc fibers andneedles may be defined as filaments the major part of which is composed of a thin elongated central spine portion consisting essentially of one or more single crystals preferentially oriented with an a axis or [010] direction) parallel to the axis of the filament, i.e., an a axis coincides with the primary direction of growth. The poly-directional side growths or branches are essentially polycrystalline and may be either granular, dendritic or platelet in form. The crys tals are generally of-irregular shape in cross-section and have a fairly large grain size as compared to conventional forms of zinc such as zinc powder. The zinc fibers and needles are substantially free of metallic impurities, containing only trace amounts of such impurities as aluminum, copper, lead and tin. The zinc fibers and needles possess a specific surface area which is intermediate that of conventional zinc powder and pyrophoric zinc sponge. The specific surface area of the zinc fibers and needles is between about,0.4 and 0.6 square meter per gram. Thelength of the zinc fibers and needles may vary from relatively short fibers of about one-eighth inch to long fibers or about 2 inches while the needles may vary from short needles of about one-eighth inch to long needles of up to about 4 inches in length. The average diameter or width of the fibers and needles is about six thousandths of an inch.

In the practice of the invention, the novel zinc fibers and needles are prepared by the electrolysis of a soluble zinc salt-containing electrolyte under conditions of extremely high cathode current density. Generally, the

The process for preparing the novel zinc'fibers and needles of the invention may be carried out in a typical electrolysis cell using a conventional zinc pig anode and a thin cathode suspended in the electrolyte bath. The fibers or needles electroform at the cathode and may be broken off and collected at the bottom of the bath or if the fibers or needles are not removed and the electrolysis is allowed to proceed, the fibers or needles tend to electrodeposit in the form of an interconnected skeletal zinc fibrous mat. This interconnected skeletal zinc fibrous'mat consists basically of multiple fibers or needles joined to one or more neighboring fibers or needles throughout the mat. By the term electroform or electroformation as used herein is meant the production of zinc fibers and needles by electrodeposition.

Galvanic cell anodes can be readily fabricated from the novel zinc fibers and needles using conventional compression molding techniques. The novel zinc fibers or needles prepared as described above are placed within the mold and then compression mold to form an anode compact of the desired size and configuration. ln forming the anode compact, the interconnected skeletal zinc fibrous mats are preferably used. If the individual zinc fibers or needles are used, it is essential that they should be thoroughly intermingled when placed within the mold. When compression is applied, the fibers or needles readily interlock or interknit with one another producing a highly cohesive anode body which is capable of supporting its own weight and retaining the shape in which it is molded.

Anode compacts fabricated as described above may be advantageously used in a variety of both-primary and secondary galvanic cell systems. Primary LeC- lanche type dry cells employing a manganese dioxide cathode may be made using an anode compact of the invention. One advantage of the anode compact in this dry cell system is that of improved resistance to leakage. The liquid cell reaction products can readily be absorbed by the zinc fibers or needles and thus become effectively immobilized within the cell.

More particularly, anode compacts fabricated in accordance with the invention are most advantageously used in both primary and secondary alkalinezinc galvanic dry cell systems. One of the principal advantages of anode compacts in such cell systems is that they afford a very high active surface area for a more efficient utilization of the anode material.

BRIEF DESCRIPTION OF THE DRAWING The invention will be more particularly understood by reference to the detaileddescription of the preferred embodiments thereof taken in conjunctionwith the accompanying drawing, wherein:

FIG. 1 is a schematic view ofa typical electrolysis cell used for preparing the zinc fibers and needles in accordance with the invention;

FIG. 2 is an isometric view showing the hexagonal crystal lattice of zinc;

FIG. 3 and are polarization curves showing the performance of surface area galvanic cell anodes made from zinc fibers as compared with conventional types of anodes known in the art;

FIG; 5 is "an elevational sectional view of a typical alkaline zinc galvanic dry cell employing an anode compact in accordance with the invention;

FIG. 6 is a perspective'view of the anode compact used in the cell of FIG. 5;

FIG. 7 is an elevational sectional view of a tyical miniature button type alkaline zinc galvanic dry cell employing an anode pellet in accordance with the invention;

FIG. 8 is a perspective view of the anode pellet used in the cell of'FIG. 7;

FIG. 9 is a graph showing the relationship between cell voltage and current of typical primary alkaline zinc manganese dioxide galvanic dry cells employing the anode compact as compared with similar cells using a gelled powder anode at various temperatures;

FIG.- '10 is a graph showing the discharge voltage of a typical primary alkaline zinc-manganese dioxide galvanic dry cell employing the anode compact as compared with a'similar cell using a gelled powder anode of the conventional type;

FIG. 11 is a graph showing the discharge voltage of a typical-primary alkaline zinc-manganese dioxide galvanic dry cell employing a gelled powder anode as compared with the potential of the gelled powder anode versus a reference electrode; and

FIG; 12 is a graph showing the discharge voltage of a typical primary alkaline zinc-silver oxide galvanic dry cell employing'the anode compact as compared with a similar cell using a gelled powder anode of the prior art.

DESCRIPTION OF THE PREFERRED EMBODIMENT FIG. 1 shows schematically a typical electrolysis cell for preparing zinc fibers and needles in accordance with the invention. The cell consists of an open tank 10 which is approximately three-quarters filled with a soluble zinc salt-containing electrolyte bath 12. Suspended inthe electrolyte bath 12 is a high purity zinc pig anode 14 such as is conventionally used in the electroplating art. A wire cathode 16, for example of zinc, is dipped just below the surface of the electrolyte bath 12. In a practical cell, an array of multiple cathodes suspended within the electrolyte bath from a common bus bar may be used, there being only one cathode shown here for the purposes of illustration. The anode 14 and cathode 16 are connected respectively through means of

wires

18, 20 into an external circuit (not shown). The circuit includes a source of direct electrical current and means such as a rheostat for controlling the flow of electrical current through the cell.

To carry out the electroformation process of the invention, the external circuit is closed suitably by means of a switch and electrical current is allowed to flow through the cell. The anode is consumed during the electrolysis forming zinc ions in the electrolyte and depositing zinc at the cathode in accordance with the following reactions:

Essentially all of the electrical current flowing through the cell is utilized in forming the zinc deposit. The cell electrolyte is invariant in that the anode is continuously replenishing zinc ions into the electrolye as zinc ions are removed at the cathode,

It has been unexpectedly found in accordance with the invention that if the electrolysis is-carried out using a soluble zinc salt-containing electrolyte of high ionic conductivity with the operating conditions of the cell being so adjusted as to provide an extremely high cath- .Ode current density, zinc fibers or needles can be electroformed at the cathode. The electroformation process is also dependent on the temperature of the electrolyte bath. It has been found that when the electroformation process is carried out at a temperature of about 25C., zinc fibers will be deposited. At higher temperatures above about 25C., zinc needles are electroformed. The temperature at which the zinc needles begin to electroform will vary depending on the electrolyte composition and the concentration of the zinc salt used in the electrolyte bath.

From the earliest experimental work leading to the invention, it was recognized that one of the essential requirements for carrying out the electroformation process is the maintenance of extremely high cathode current densities. It has been found in accordance with the invention that the cathode current density should be maintained at about a least 500 amperes per square foot. In the preferred practice of the invention, the cathode density should be maintained at about 1,000 amperes per square foot. This is considerably higher than that used in the conventional electroplating art for depositing smooth coatings of zinc from an alkaline zinc cyanide bath wherein cathode current densities of from about to 50 amperes per square foot have been reported (Electroplating Engineering Handbook by A. K. Graham, page 214, Reinhold Publishing Company). In the production by electrolytic methods of dendritic zinc sponge according to the Clark et al. patent, supra, cathode current densities of only about 140 amperes per square foot are required. Since the current, density is inversely proportional to the cathode surface area for agiven current, it is advantageous to employ a cathode of the smallest practical surface area exposed to the electrolyte and preferably a very thin wire cathode is used. During the electroformation process, the zinc first deposits at the cathode in the form of individual fibers or needles which may be easily broken off and then collected at the bottom of the electrolyte bath. If the process is allowed to proceed without removing the individual fibers or needles, the electroformation will continue with more and more fibers or needles being deposited from the initial growth at the cathode surfaces. The growth of more and more fibers or needles will continue in this manner so long as sufficient electrical current is flowing through the cell to promote the electrodeposition of the fibers or needles and eventually an interconnected skeletal zine fibrous mat will be formed. This skeletal fibrous mat consists basically of multiple fibers or needles joined to one or more neighboring fibers or needles in the mat.

Once the electroformation process has been started and the formation of the interconnected skeletal fbrous mat has begun, it may be necessary to periodi cally increase the flow of electrical current through the cell, such as by means of the rheostat, in order to meet the increased current requirements due to the increasingly greater number of fibers or needles being deposited. It is virtually impossible during this period of the process to determine the cathode current density with any degree of accuracy due to the rapidly changing surface area of the zinc deposits. However, the electroformation process may be expediently carried out by properly controlling the amount of electrical current flowing through the cell to provide an estimated cathode density which is above the minimum requirement to promote the electroformation of the fibers or needles. The proper range of cathode current density can be estimated simply by visual observation of the type of deposit or reaction occuring at the cathode. If the cathode current density is too low, no fiber or needle deposits can be observed. The deposit in this instance will be of the level, adherent type or the powdery type. If the cathode current density is too high, gas evolution (hydrogen) will be readily observed.

In the practice of the invention, the electrolyte may contain any zinc salt whose principal requirement is that it be soluble in a solvent of high dielectric constant resulting in a solution of sufficient ionic conductivity to permit the maintenance of at least the minimum cathode current density necessary for electroforming the zinc fibers and needles of the invention. 7

Suitable soluble zinc salts include the acetate, bromide, chlorate, chloride, formate, iodide, l-phenol-4- sulphonate, sulphate, thioeyanate, borate, bromate, fluogallate, fluoborate, fluosilicate, glycerophosphate, nitrate, phosphate, and sulphonate. Suitable solvents for the zinc salt include water, alcohols such as metha nol, ethanol, and n-propanol, nitromethane, propylene carbonate and dimethylfor'mamide. Cost and conductivity considerations are the two most important factors upon which the choice of the zinc salt and solvent should be based. Zinc chloride and zinc sulphate are the two preferred choices for the zinc salt from the standpoint of cost and conductivity. An aqueous solu tion of zinc chloride is the most preferred electrolyte solution. Water is the preferred solvent because of its low cost and freedom from fire hazard and toxicity. An additional salt such as ammonium sulphate may be used to increase the conductivity of the electrolyte bath.

The concentration of the soluble zinc salt in the electrolyte solution is not too narrowly critical so long as enough zinc ions are present in .the electrolyte to promote the electroformation of the zinc fibers and nee dles and further provided that a suffieiently high conductivity is maintained. Generally, the electrolyte solution should contain at least above about 30 per cent by weight of the soluble zinc salt in solution.

As indicated above, it has been found that while the zinc fibers of the invention may be electroformed at a temperature of about 25C. under the conditions of extremely high cathode current density, elevated temperatures of above about 25C. are required to form the zinc needles and that the specific temperature at which the zinc needles will begin to deposit will vary depending on the electrolyte composition and the concentration of the soluble zinc salt used To illustrate, it has been found that whereas zinc fibers will be electroformed at a temperature of about 25C. using a 47 per cent by weight solution of zinc chloride in water, the temperature of the electrolyte must be elevated to about C. before Zinc needles will be deposited. With basically the same electrolyte solution but using methanol as the solvent, zinc needles will be deposited at a temperature of about 40C. It will be appreciated that determination of the temperature at which the zinc needles will be electroformed in accordance with the invention for any given electrolyte composition and concentration of the zinc salt is a simple matter of routine experimentation and that such experimentation is well within the ability of one skilled in the art. I

An important feature of the electroformation process of the invention is that the individual zinc fibers and needles may be advantageously 'varied in length by properly controlling'the cathode current density, that is, by adjusting the amount of electrical currentflowing through the cell. It has been found that in addition to the temperature of the electrolyte bath, the v current density maintained at the cathode has a profound influence on the natureof the zinc deposit and specifically the maximum lengthto which the respective individual fibers or needles may grow. By varying the electrical current flowing through the cell and consequently the cathode current density, the length of the fibers or nee dles may be varied from relatively short to long fibers or needles. The length of the fibers or needles will vary in inverse proportion to the cathode current sothat by increasing the cathode current the length of the fibers or needles will be decreased and conversely by decreas ing the cathode current the length of the fibers or needles will be increased. It will thus be seen that long, medium and short fibers or needlesmay bereadily prepared. The zinc fibers maybe prepared in lengths ranging from relatively short fibers of about one-eighth v,inch to long fibers of about 2 inches in length while the zinc needles may be prepared in lengths ranging from relatively short needles of about one-eighth inch to long needles of up to 4 inches in length. v

Y Table 1 below illustrates the effects of both temperature and cathode current upon the nature of the zinc deposit. The electrolyte solution used to obtain the data shown in the table was a 47 per cent byweightso; lution of zinc chloride in water. Zinc needles electroform at a temperature of about 80C. using this electrolyte.

- TABLE I EFFECT OF TEMPERATURE AND CATHODE CURRENT UPON THENATURE OF ELECTROFORMED ZINC Approx. Tempera- Form of Length ture Cathode Current Ele'ctroformed Zinc inches C. Amperes Short Fibers Va A 25 65 300 Long Fibers l 25 80 Very Long Fibers l 2 25 l5 Short Needles I A; A 90 I Long Needles l 90 50 Very' Long Needles 2 These data dramatically show the effects of varying both the temperature and the electricalcurrent'flowing throughthe cell. As shown in the table, 'thetempera measured because'of the rapidly changing surface area of the zinc deposits but the current'density was estimated to be well above about 500 amperes per square foot.

To illustrate'the practice'of the invention, zinc fibers havebeen prepared using an electrolysis cell similar to that shown in FIG. 1 except'that two arrays of seven thin zincwire cathodes of about 0.312 inch in diameter dipping approximately 0.2 inch into the electrolyte solution were used, one array" on each side of a zinc pig anode. The electrolyte was a 47 p er cent by weight solution of zinc chloride in water an'd the anode-to cathode distance wasabout 5 inch'esfThe temperature of the electrolyte was 'maintained a't' about 25C. Upon closing the electrical circuit, a current" of about 180 amperes flowed 'th'ro gh the cell and zinowas observed to electrodepos'it at the cathode surfaces in the form of individual fibers. Th fibers formed initially at the higher current density edges of each cathode and could be easily broken off immediately as they were formed by scraping the surfaces of each cathode, the fibers then falling'to the bottom of the electrolyte bath. When the electrolysis was allowed to proceed without removing the fibers, more and more fibers were observed to electrodeposit from the surfaces of the fibers initially formed at each cathode and this process continued with each of the fibers joining to one or more neighboring fibers until an interconnected skeletal zinc fiber mat was pr oduced. Eventually the weight of 'the fiber that so produced cau'sed it to be broken off from the cathode surfaces and the inat then fe ll to the bottom of the electrolyte bath. The process was continued to produce more and more fibermat. i

Zinc needles have also been prepared using the same electrolyte composition as disclosed in the above example/The process was carried out under essentially the same'conditions except that the electrolyte was maintained at a temperature of about C.

' Crystallographiestudies have been made in order to determine the crystal structure of the zinc fibers and needles of the invention. It is known from the literature that the zinc crystal is a hexagonal lattice composed of three unit cells. FIG. 2 shows diagramatically this hexagonal latticefor zinc with one of the unit cells'bein'g shown in darkened outline'for purpo'ses of illustration. It will be seen from the drawing that there are twozinc atoms to the unit cell. The unit cell is composed of 'oneeighth of a-zindatom of eachof the corners and one zinc atom at a location within the cell. Each corner atom is shared by eight unit cells of adjacent crystals. The" two axes of the zinc lattice'are identified as the a and c axes in the literature and are shown in the diagram of FIG. 2. v I

An X-ray diffraction pattern for conventional zinc powder shows'continuous lines representing the randornness of crystal orientation and polycrystalline nature in the' zinc powder. v

X-ray diffraction data have been" obtained for 'the zinc fibers and needles of the invention. These datawere obtained bythe rotating crystal method/The fibers and needles were mounted with their growth direction, i.e., direction along their length, perpendicular to the impinging X-ray beam.

The X-ray diffraction pattern for the fibers shows the characteristic spots arranged on layer lines when the crystal is aligned withits growth axis perpendicular to the Xray beam. i I 1 The'identity or repeat distance along this crystal growth axis can be calculated from "the distance between'tlie layer lines on the film and was found for both the fibers and needles to be 2.665A. This is the same value published in the literature 'for the distance between zinc atoms along the a axis of the crystal. It will erentially' orientated with ana axis or [010] di- TABLE II X-RAY DIFFRACTION DATA FOR ELECTROFORMED ZINC FIBER Observed location of. reflection on Zn fiber orientated with its long Intensity direction perpendicular d (Powder Data) hkl to impinging Xray beam 2.473 53 002 layer line only 2.30 40 I00 0 and lst layer lines 2.09l I00 l0] 0 and lst layer lines L687 28 I02 0 and lst layer lines L342 25 103 0 and lst layer lines 1.332 21 H0 lst layer line only L237 2 004 0 layer line only 1.1729 23 H2. lst layer line only 1.1538 200 0 and second layer lines 1.1236 17 201 0 and second layer lines 1090] 3 I04 0 and lst layer lines 1.0456 5 202 0 and second layer lines Theoretically, if the fibers are composed of more than one crystal and they have preferred orientation along the a axis ([100] or [010] direction), 11 and/or k =0 on the zero layer line and 11 and/or k l on the first layer line. It will be readily seen from the table that the observed data agree with the theoretical.

Crystal grain studies have also been made on the zinc fibers and needles of the invention. The data obtained were compared with results of similar studies conducted on conventional zinc powder. All of the specimens studied were mounted, sectioned, polished and etched to bring out the grain structure. In the case of the zinc fibers and needles, the specimens were all sectioned through a plane taken in a direction perpendicular to the central spine portion of the fibers and needles.

Crystal grain size measurements were taken on the zinc fibres in a direction essentially perpendicular to the growth axis and thecrystals were found to range in size from the largest grain diameter of about 0.01 inch to the smallest grain diameter of about 0.0002 inch (2 X The average grain diameter of the crystals was determined to be about 0.005 inch.

Crystal grain size measurements were taken on the zinc needles and the crystals were found to range from the largest grain diameter of about 0.002 to the smallest grain diameter of about 0.000] inch. The average grain diameter of the crystals was found to be about 0.0008 inch.

Crystal grain size measurements were taken on the zinc powder and the grain diameter was found to range from about 0.000004 to 0.001 inch. The average grain. diameter of the zinc powder was found to be about 0.0002 inch.

Zinc fibers and needles prepared in accordance witharea which is far in excess of that of conventional zinc powderbut which at the same time is not so highly. developed as to be pyrophoric and susceptible to rapid oxidation upon exposure to the atmosphere. Moreover, the fibers and needles contain. only trace amounts of impurities and consequently they are less prone to the formation of local corrosion couples resulting in wasteful corrosion of the anodes and gassing during storage ofthecells. 'f

Surface area measurements of the zinc fibers and needles have been taken using the krypton absorption BET method.* The fibers and needles were found to possess a specific surface area between about 0.4 and 0.6 square meter per gram. Conventional zinc powder using the same method was found tqpossess a specific surface area of only about 0.016 square meter per gram. .It will thus be seen that the zinc fibers and needles have more than 30 timesmore surfa ce area per unit weight than does the powder. Zinc sponge has a specific surface area many timesthat of the zinc fibers and needles (approximately 4 to 7 square meters per gram) but is highly pyrophoric. The advantage, of the zinc fibers and needles is that they possess a considerably higher specific surface area than does the zinc pow: der without the disadvantage of rapid atmospheric oxidation observed with the higher surface area zincsponge. g g V *BET method Journal of American Chemical Society, Vol. 60, pg. 309, 1938, S. Brunauer, P. H. Emmett and E.-Teller.

Qualitative spectrographic and colorimetic analyses have also been conducted on the zinc fibers and nee dles of the invention. These studies have demonstrated thatthe fibers and needles are one of the purest forms of zinc obtainable within a reasonable economic frame work. The electroformation process is accompanied by electropurification and it has been found that the zinc fibers and needles so produced contain only trace amounts of impurities such as aluminum, copper, lead and iron. Table III below shows the resultsof the spectrographic analysis for impurities in zinc fibers as compared with conventional zinc powder. It will be readily seen from the table that the zinc powder contains minor amounts of both lead and iron while the zinc fibers contain only trace amounts of these impurities. i

'TABLE in QUALITATIVE SPECTROGRAPHIC ANALYSIS Zinc Fibers Electroformed from Pig* Major +Minor +Trace- Major- Zinc Powder *Zinc Pig purity 99.990/zinc 0.003% lead (max). 0.00l71 iron (max). 0.003% cadmium (max).

1 1 zinc such as zinc pig, two commercial types of powder, and-zinc sheet.

I TABLE IV zinc QUALITATIVE COLORIMETRIC ANALYSIS FORIRON (Accuracy of method is i 0.5 ppm) High purity is important from the standpoint of re ducing gassing couples formed betweenthe zincan d other metals present as impurities. Iron is a good exampleof a metal which forms a gassing couple with zinc in alkaline media. It will be seen from Table IV that there is a significant reduction in iron concentration in the zinc fibers and needles as compared wih the other forms of zinc analyzed. The zinc sheet contained the greatest concentration of iron of about 18 ppm while the two samples of zinc powder contained 6.5 and 1 1 ppm respectively. It will be seen that the zinc fibers and needles represent the purest form of zinc containing only" about 1.5 ppm of iron and thus would result in substantial reduction of gassing and wasteful corrosion of the zinc anode in a galvanic cell.

High surface area anodes'for use in galvanic cells maybe readilyfabricated using the zinc fibers and needles of the invention by conventional compression molding techniques. The individual fibers or needles are placed within a suitable mold of the sizeand configuration desired and then compressed under a suitable pressure, say about 40 psi. Before applying pressure, the fibers or needles should be thoroughly intermingled with one another so that they are arranged in randomly orientated fashion within the mold with each of the fibers or needles making contact with as many neighboring fibers or needles as possible. It will be readily seen that the interconnected skeletal zinc fiber mat produced in accordance with the invention is advantageous for use in this molding procedure since the fibers or needles are thoroughly intermingled and joined to one or more neighboring fibers in the mat. Upon the application of pressure, the intermingled fibers or needles readily interlock or interknit with one another producing an anode compact of high strength and cohesiveness.

Anode compacts so produced have been found to possess a number of advantages over anodes of the prior art. They possess a high strength and cohesiveness and are capable of supporting their own weight and consequently they do not require the use of a gelling agent such as carboxymethyl cellulose as employed in conventional gelled powder anodes. More-over, the zinc fibers and needles contain only traee amounts of metallic impurities and therefore there is less tendency for the establishment of local corrosion couples which might otherwise result in wasteful anode corrosion and gassing during storage of the cells. g

A series of polarization tests were conducted in order to demonstrate the superior performance'capabilities of anode compacts made in accordance with the invention. The performance of the anode compacts was compared in the test with that of conventional flat zincsheet anodes, sprayed zinc anodes (molten zinc sprayed onto a perforated zinc grid), and gelled powder anodes consisting of-zin'c powder suspended in a carboxymethyl cellulose gel. The anode compacts used in the test were made from zinc fibers electroformed from a methanol solution of zinc chloride. The weight of zinc was the same (0.80 gram) in both the anode compacts and gelled powder'anodes tested. The tests were performed in a polytetrafluoroethylene cell holder using a large excess of a 35.8per cent by weight potassium hydroxide electrolyte solution containing 4.48 per cent by weight of zinc oxide. The anodes were held in a vertical position with an anode face of about 0.78 square inch of apparent area exposed to the electrolyte. A large zinc cathode and a cadmium reference electrode were used in the cell. Current was provided by a 60-cycle a.c. interrupter of the type disclosed in the Kordesch et al publication, (Journal of the Electrochemical Society, vol. 107, pages 480-483, June 1960 Substantially resistance-free potential readings were taken and recorded. A Keithley electrometer was used to make these readings.

Polarization curves for all the anodes tested at a tempeature of 25C. are shown in FIG. 3. 'Both the anode compacts and gelled powder anodeswere also tested at low temperatures of about 20C. and the polarization curves obtained in these tests are shown in FIG. 4. Each of the curves plotted represents the average of three individual runs. The drop in potential measured at a given value of current below the potential obtained with no imposed anodic current is interpreted as being largely due to concentration overpotential although an activation overpotential component is included. The

point in the curve where the potential experiences a sudden drop downward is taken as theljmiting current, i.e., i,,-,,,. It will be seen from the polarization curves in FlGS."3and 4 that the anode compacts of zinc fibers exhibited superior performance under conditions of high rate discharge and low temperature as compared with the other types of zinc'anodes tested.

FIG. 5 shows a typical alkaline zinc galvanic dry cell employing an anode compa'c't made in accordance with the invention. The cell comprises a cupped metallic can 22 surrounded by an insulating jacket 24. The extremities of the jacket are crimped around the outer edges of an insulated top cover 26 and an outer bottom metal cover 28. A paper washer 30 electricallyinsulates the can 22 from the bottom cover-"28. Snugly fitted within the can 22 is a tubular cathode 32, the innermost surfaces of which are lined with a paper'separator 34. Secured to the top of can 22 .is a metal cap 36 serving as the positive cathode terminal.

The cathode used in the cell maybe composed of manganese dioxide or other oxidic depolarizer material. Preferably, the cathode is of the cement-bonded type such as disclosed and claimed in U.S. Pat. No. 2,962,540 issued to K. Kordesch on Nov. 29, 1960.

Separated from the top of can 22 by means of separator 34 and the plastic insulating disc 38 is the anode compact 40-of' the invention. The anode compact is made by compression molding the zinc fibers or needles into cylindrical form as more particularly shown in FIG. 6.

The electrolyte for the cell is suitably a concentrated solution'of potassium hydroxide, i.e., 30 to 35 per cent by-weight solution-of KOH. The electolyte is absorbed into the anode compact and soaks the separator 34.

Suitably the closure for the cell may be of the type disclosed and claimed in U.S. Pat.'No. 3,042,734 issued to J. L. S. 'Daly et al. on July 3, 1962. Such a closure comprises an inner metalbottbm 42 sealed within the open end of can 22 by means of a nylon gasket 44 having a central opening'46. This opening is of a diameter slightly smaller than the external diameter of a rivet 48 so that when the rivet is driven through the opening 46 the gasket will be radially compressed between the inner bottom member 42 and the rivet head,,thereby furnishing a tight mechanical seal thereat. Prior to driving rivet 48 through the cover and gasket, the same is passed through a central opening and in the anode col lector 50. This anode collector may be formed by a pair of rod-like members 52 formed integrally with a head plate 54 in which the central opening is provided for the rivet 48, the pair of rod-like members 52 being embedded within the anode compact 40.

Illustrative of the practice of the invention, an anode compact for use in a D-size alkaline zinc-manganese dioxide galvanic ,dry cell of a construction such as shown in FIG. may be made by compression molding 15.5 grams of zinc fibers into a cylindrical shape approximately 1.6 inches high and 0.85 inch in diameter. Such an anode compact has a void volume of about 85.8per cent of the total volume which is more than sufficient for the subsequent absorption of the electrolyte.

FIG. 7 shows a typical miniature button type alkaline zinc galvanic dry cell employing an anode compact of the invention. The cell comprises a metallic cup 56 which serves as the positive terminal. Within the cup 56 and in contact with its bottom wall is a thin wafer-like cathode 58. The cathode may be composed of any oxidic depolarizer material such as manganese dioxide, nickel oxide or silver oxide, for example. The anode is in the form of a thin pellet 60 and is disposed on top of thecathode 58 separated therefrom by at least one layer of a suitable separator material 62. A metallic top closure 64 is placed within the open end of the cup 56 and is pressed downwardly into contact with the top of the anode pellet 60. The top closure 64 is sealed around its outer periphery by a generally L-shaped plastic insulating grommet 66 and serves as the negative terminal of the cell.

The anode pellet used in the button type cell of FIG. 7 is made by compression molding the zinc fibers or needles as described hereinabove. FIG. 8 shows the anode pellet prior to assembly in the cell.

One of the most outstanding features of the invention is that the anode compacts can be readily fabricated using the zinc fibers and needles without the need for any suspension or gelling agent such as used in gelled powder anodes of the prior art. The elimination of the gelling agent is highly advantageous from the stand point of providing optimum volumetric cell efficiency since the gelling agent used in prior anodes i.e. carboxymethyl cellulose ,.is electrochemically inactive and performs no useful purpose other than to support the zinc powder. Its elimination thus allows for more active material to be incorporated into the anode structure and consequently the cell discharge capabilities are substantially increased.

Still other advantages are derived from the elimination of the gel in sealed secondary or rechargeable alkaline zinc galvanic dry cells. It has been found that the carboxymethyl cellulose gel is readily oxidized and tends to break down upon repeated cycling, that is, charge and discharge, and thus destroys the mechanical integrity of the anode body. It has been furthermore found that the presence of carboxymethyl cellulose in concentrated potassium hydroxide electrolyte contain ing zincate results in hydrogen gas evolution at the zinc interface during charging. The degree to which this reaction occurs is directly dependent on the concentration of carboxymethyl cellulose. The exact nature of this reaction has not been established but it is thought that it may be associated with the transport of zincate ions to the metal interface where reduction takes place, i.e., the carboxymethyl cellulose renders it more difficult for the zincate ions to reach the site for reduction. Another serious problem encountered with prior gelled powder anodes is that, under conditions of overcharge, the gel network tends to prohibit rapid oxygen recombination with the anode material and consequently dangerous internal gas pressures may develop in the sealed cells.

A series of experiments have been conducted to demonstrate the superior performance of alkaline zinc galvanic cells usinganodes fabricated in accordance with the invention. In one such experiment, a number of D- size primary alkaline zinc-manganese dioxide dry cells were made, somewith conventional gelled powder anodes i.e., zinc powder in a carboxymethyl cellulose gel, and others with anode compacts of compressed interlocked zinc fibers fabricated in the manner as set forth hereinabove. The same amount of zinc was used in both types of cells i.e., the zinc fibers were equivalent in weight to the zinc powder used in the gelled powder anodes. A 41 per cent by weight solution of potassium hydroxide was used as theelectrolyte in all of the cells tested. Performance of the two types of cells was compared by progressively switching each of the cells for l5-second intervals across load resistors of 10, 2 l, 0.5, 0.337 and 0.252 ohms. The voltages were continuously recorded on a potentiometric recorder. The voltage at the end of each l5-second interval was then used to gether with the known load resistor to calculate the current. Testing was conducted at temperatures of 25C., 0C. and 20C. The voltage versus current relationship of the cells tested is shown in FIG. 9. It will be readily seen that for all the temperatures at which the cells were tested, the cells employing the interlocked zinc fiber anode compacts exceeded the performance of the cells employing the gelled zinc powder anodes of the prior art.

In another series of experiments, the superior performance capabilities of a primary alkaline zinc-manganese dioxide dry cell employing a zinc fiber anode compact versus an identical cell using a gelled zinc powder anode under conditions of heavy drain discharge were demonstrated. Again the same weight of zinc was used in both types of cells and the cells were otherwise identical in that they employed the same type of cathode, electrolyte and separator. During the test, the cells were continuously discharged across a l-ohm resistor. A comparison of the discharge voltage of the two types of cells tested is shown in FIG. 10. The discharge curves for both cells are essentially the same during the first six hours of discharge. At this time, however, a rapid drop in cell voltage was observed from the cell employing the gelled .zinc powder anode. When duplicate cells employing the gelled anode were tested, a similar rapid drop in cell voltage was observed although the time at which this drop occurred varied from 4.5 to 6 hours depending upon the individual cell. It will be seen that there is no rapid voltage drop in the discharge curve for the cell employing a zinc fiber anode compact but rather the drop in voltage is gradual throughout the period of test. i I

The rapid voltage drop observed with the dry cells employing the gelled zinc powder anode on l-ohm discharge after 4.5 to 6 hours was associated with the polarization ofthe anode. On the other hand, practically all of the cell voltage decline previous to this time was associated with the polarization of the manganese dioxide cathode. In order to demonstrate thisa reference electrode was placed in one of the cells employing the gelled powder anode and the potential of the working electrodes was recorded while the cell was continuously discharged across the 'l-ohm resistor. FIG. 11 shows the gelled zinc powder anode potentialand compares this with the cell voltage on discharge. Similar potential measurements between a reference electrode and each of the two working electrodes in a cell employing a zinc fiber anode compact indicate that essentially all of the cell voltage decline on one-ohm discharge is associated with polarization of the manganese dioxide cathode.

The following conclusions'can be drawn from the through the electrolyte from the catho'de to the anode.

the ,c'ellsare hermetically sealed inorder to prevent the above seriesof experiments comparing thedischarge a. Essentially all of the cell-voltage declineto 0.7 volt is due to the polarization of the manganese'dioxide cathode. Only about 0.1 volt can be attributed to the polarization of the zinc anode.

b. Essentially all of the rapid voltage drop that occurs between 0.7 volt and 0.1 volt is due to the polarization of the gelled zinc powder anode.

(II). For zinc fiber anode'cells;

a. No rapid polarization of the zinc anode comparable to that seen with the gelled zinc powder anode cells is observed at 0.7 volt.

b. Essentially all of the decline in cell voltage over the first 20 hours of discharge is associated with the polarization of the manganese-dioxide cathode. Cell capacity is limited by this polarization and could be improved by use of a superior manganese dioxide cathode material.

III. Substitution of the zinc fiber'anode for the gelled anode in an alkaline zinc-manganese dioxide dry cell results in increasing the cell capacity during the first 20 hours of discharge'(FIG. '10) from 5.9 to 10.3 ampere hours. The additional capacity is obtainedat cell voltages below O.7 volt due to'the polarization of the manganese dioxide cathode which masked the true capability of the zinc fiber anode as far as the cell potential is concerned. In spite of this, however, the zinc fiber anode demonstrated its capability to sustain high rate discharge for much longer periods of time than the gelled 'zinc powder anode.

In' the manufacture of prior alkaline zinc galvanic dry" cells of the type using a gelled zinc powder anode, it has become the common practice to amalgamate the zinc powder priorto formation of the gelled anode. This is necessary in order to prohibit thecvolution of gas generated particularly during storage of the cells due to the establishment of local corrosion couples formed be tween thezinc and other metals present as impurities. As indicated above, iron is a good example of a metal which forms a corrosion couple with zinc although established with zinc by the migration of impurities other metal impurities are capable of forming such couples in the alkaline media. Gassing couples can also be loss of.electrolyte dueto leakage or evaporation. With such sealed cells it" is generally necessary to provide some means to adequately venting the gases formed by these corrosion or gassing couples as well as those gases generated during use of the cell such as upon charging or overcharging iri the case of a rechargeable cell, for example. I i r Amalgamation of the 'zincpowder prior to fabricating the gelled powder anode with usually about 8 per cent by weight of mercury has proven effective in prohibiting or substantially reducing the evolution of gas caused'by the establishment of local gassing couples due to the presence of'impurities in the line. It has now been found, however, that the level of amalgamation required with the present anodes may be reduced below that necessary with the gelled powder anode. This is at least partially due to the fact that the'zinc fibers and needles contain only trace amounts of impurities, notably iron for example. Reduction inthe level of amalgamation in the case of the present anodes, however, depends largely upon the nature of the cathode material. If the cathode material contains only'alimited amount of major impurities which might'otherwise migrate through the cell electrolyte to the anode and establish local gassing couples thereat,then the level of amalgamation in the case of the present anodes may be substantially reduced below that required for the gelled powder anode.

' In order to demonstrate the possible reduction in the level of amalgamation for anodes made in accordance with invention, another series of experiments was conducted using D-size sealed alkaline zinc-maganese dioxide galvanic dry cells. In these experiments, the cells were constructed without the standard manganese dioxide cathode so as to effectively isolate the anode and its electrolyte. Any-gas evolution occurring during the test was thus solely attributable to the establishment of local corrosion or gassing couples due to impurities in the anode. A total of 26 cells were used in the test; The

cell closures were modified to accommodate a pressure gauge so that the internal gas pressure could be determined at any time during the test. The anodes were fabricated from compressed interlocked zinc fibers or needles, some of which were unarnalgamated and other of which were amalgamated with various amounts of mercury up to 8 per cent" by weight of mercury. Amalgamation was accomplished from an ethylene diamine complexof mercury. The weight of zinc fibers or needles for all the anodes was the same i.e., 15.5 grams, and the anodes were cylindrical as shown in FIG. 6. A 41 percent by weight solution of the potassium hydroxide was used-as'the electrolyte for all the cells and the electrolyte volume 'was the same i.e.,' 12.8 milliliters. The electrolyte was previously shaken thoroughly with zinc fibers for the purpose of removing any trace heavy metal impurities that may have been originally present in the potassium hydroxide solution. A control lot of cells similar to those just described was constructed using a standard gelled powder anode i:'e., zinc powder suspended in a carboxymethyl cellulos'e' gel. The weight of the zinc powder was equivalent to that of the zinc fibers or needles used in'mak'ing the anode compacts and the zincipowder wasamalgamated with the standard 8 per cent by weight of mercury; The testcells were then placed in the bottom of a Pyrex beaker filled with par-2 affin oil so that any leaks in the sealed cell system could be easily detected bygas bubbling through the paraffin oil. A Pyrex tube having an open bottom and. and

a 18 with at least.3.per cent or more of mercurly rernained below themaximum selectedlevel. It should be understood, of course, thatqthe se experimentswere carried out under conditions wherein the effect of cathode imequipped with a stopcock was placed withinthe beaker purities was deliberately circumvented by eliminating surrounding the cell and its pressure gauge. An cxthe cathode from each of the cells tested. Migration of tremely sensitive pressure test apparatus was thus pro a substance or substances originating as. impurities in vided for measuring the quantity of gas evolvedfrom the cell cathode to the zinc' anode withsubsequent esthe cells. The sensitivity of the measurements was extablishment of gassing couples can account for the ceedingly high in that 7 X moles of gas could" be 10 major source of gassing in an alkaline zinc-manganese easily detected. This is equivalent to '1 .4 X l0 grams dioxide galvanic dry cell. Thus when'a. cathode of poor of hydrogen or a local couple current of 0.2 milliamquality is used it may be necessary with anodes ofthe pere-hour magnitude. The cells were then placed on invention to substantially increase thelevel of amalgashelf storage within the test apparatus and we're sepamation .above the lower percentage demonstrated as rated into two groups One group of cells was mainfeasible in theseexperiments. l tained at a temperature of 24C: While'the other group Many different types of alkaline zinc galvanic cells was maintained at a temperature of 54C. Pressure data have been made using anodes fabricatedfromthe zinc wereperiodically obtained by fm easuring the quantity fibers and needles in accordance with thesinyention. of gas evolved from the cells. The test was carried out Besides. the primary alkaline zinc galvaniodry cells for a period of up to 2 1/2 years. Table V below sumused in the above experiments, a number of secondary marizes the tesults of'thesetests. or rechargeable galvanic-drycells alsohave beencon- .TABLEV,

l 'ANODE SHELF DATA Pressure (Psig) After; Pressure (Psig) Storage at 24C. After Storage (months) a at 54C. l. I a l Q (months) Unamalgzlmated 7 15 20 27 33 l00 Zinc Fibers Amalgamated (0.28% Hg) 0 7 l2 19 25 l()0 V Zinc Fibers Amalgamated (0.28% Hg) 0 2 I 7 14 20 100 v Zinc needles Amalgamated (2.0% Hg) .0 0 Zinc needles l a Amalgamated (3.0% Hg) 7 U O v 4 Zinc needles Amalgamated (4.07: Hg) 0 2 line needles Amalgamated (51)7? Hg) 0 2 Zinc needles Amalgamated (6.0% Hg). 0 (l I 0 Zinc needles Amalgamated (7.07: Hg)- 0 O .0 Zinc needles V Amalgamated (8.0% Hg) 4 5 5 s 5 l0 Zinc needles Amalgamated (8.0% Hg) 0 0 "0 7 s s a s 12 Zinc Powder CMC a Anode gel It will be readily seen that the results shown in Table structed. These cells differ from those. of primary type V amply demonstrate that the level of amalgamation only in the specific composition of the cathode material for the anodes of the invention can be effectively re; and the electrolyte. M l l duced to aslow as about '3 percent by weight of mer- .Rechargeablealkaline zinc-nickel oxide galvanic dry cury provided that a good quality cathode containing a cells employingthe anode of the invention have .been minimum amount of impurities is used. Pressure readtested for prolonged periods of time with repeated cyings of about 40 psi were selected as the maximum cling i.e., charge and dischargepand have shownasupepressure to be tolerated in the alkalinezinomanganese rior performance in that the cells were capable of atdioxide galvanic. dry cells. Those cells, in which the zinc taining a state of full charge. afteradischarge over a fibers or needles were unamalgamated or amalgamated greater number of cycles than possible with rechargewith'only up to 2 .weight per cent mercury gassed profuselyafter 2 years of storage. On the. other hand the.

gas pressure in the cells constructed with anodes in which the zinc. fibers or needles -were amalgamated able cells employing the conventional gelled zinc powder anode. This is believed due to .the fact that the anode of the invention more readilypermits rapid oxygen recombination with the active material since there .oxidizable organic gelling agent is 'pres'ent to deteriosembled in the cell container in the dry='state"follo'wed by metering of the desired amount of electrolyte rather than by the more complicated procedure of meteringa wet gelled powder anode into the cell container/More over, there is less tendency for leakage of the electrolyte which is a major problem with these button type cells since the anode pellet .is highly absorbent and soaks up andholds the'electrolyte.

As further illustrative of the=invention; a number of miniature button type primary alakline zinc-silver oxide galvanic dry'cells employing an anode pellet in accordance with the invention have been made and tested. The "cells were subjected to a continuous discharge across a 600 ohm load resistor. FIG. 12 shows the discharge performance at room temperature of such a cell compared with the performance of a similar cell using a gelled zinc powder anode.

In the manufacture of conventional rechargeable alakaline zinc galvanic dry cells, it is common to em ploy an electrolyte consisting of a concentrated solution of potassium hydroxide, suitably a 30 to 35 per cent solution of KOl-I. It has now been found, however, that with such rechargeable dry cells employing the anode of the invention the cycle life can be substantially increased by using a more highly concentrated solution of potassium hydroxide together with a high concentration of zinc oxide dissolved therein. Specifically, the molar ratio of KOI-I to ZnO should be of the order of about 6 to 1. Analysis of these electrolytes falls in the range of about 45 to 50 per cent potassium hydroxide and 12.5 to 15 per cent zinc oxide. The improved performance of these electrolytes can be attributed to the reduction in the formation of zinc dendrites formed during cell charging.

With the electrolytes contemplated in accordance with the invention, the formation of zinc dendrites on charging may be substantially reduced and the cycle life of the cells significantly improved. It has been furthermore found that the formation of these zinc dendrites may be even further reduced by incorporating in the cell electrolyte one or more additives selected from the group consisting of lead, arsenic, molybdenum and tungsten. In the alkaline solution, these additives will be present as the plumbite, arsenate, molybdate and tungstate. These additives should be present in the cell electrolyte in-an amount of at least ppm although a concentration of at least 1000 ppm is preferred.

Ideally them-electrolytes most suitablefor use in rechargeable alkaline zinc galvanic dry cells employing an anode made in accordance with the invention are highly concentrated solutions of 40 to 45.per centtpo tassium hydroxide containing-about l2.5'-to 15 per cent zinc oxide dissolved therein and having added thereto,

in an amount of at least 20 ppm one or more additives selected from the group consisting of lead, arsenic, m'olybdenum, and tungsten. 1

When using-the above electrolytes in a rechargeable" alkaline zinc galvanic dry cell, it has been found prefer- 20 abl'e'to employ a separator system consisting of multiple layers of a non-woven open pore material which is highlyretentive of the electrolyte. This separator system is resistant to the penetration of zinc dendrites formed at the anode and thus serves to further improve the cycle life' of the cell. Suitable separator materials for'this purpose include Viskon-Vinyon* or other synthetic. fiber batts.

*Viskon-Vinyoncomposi te separator consisting of cellulosic fiber material and a copolymer of vinyl chloride and vinyl acetate.

v A numberfof miniature button type rechargeable al kaline zinc-nickel oxide galvanic dry cells utilizing the electrolytes of the invention have been made. The cell constructionwas basically the same as that shown in FIG. 7. Theanodes for each cell were fabricated by compression molding zinc-needles into the form of a wafer-like pellet (FIG. 8). The electrolyte composition was varied from a standard'solution of 35 per cent :KOl-I plus 1.5 per cent ZnO'to' electrolyte compositions containing 47.5 per cent KOH and 12. 5 per cent ZnO with and without the addition of 1000 ppm of lead. The

separator usedin the cells employing the electrolytes of the invention consisted of ten layers of 0.008inch Viskon-Vinyon. -The cells were subjected to deep discharge to 0.9 volt at the l /2 hour rate followed by constant current charging at the 4-hour rate plus 50 per cent minimum overcharge. The cells were considered to' have reached the end of their useful cycle life when the cell capacity dropped off to 50 per cent of the initial capacity. Table VI below shows the results of these tests.

TABLE VI EFFECTS OF ELECIROLYTE ADDlTlVES Electrolyte Composition Cycle life to 50% of Initial Capacity 7 A. 35% KOH 1 /2 ZnO l2 B. 47% KOH 12 /2% ZnO 65 c. 47% KOH 12 /2% ZnO 1000 ppm 129 Pb (added as PbO) It will be readily seen from the tableabove that the electrolytes of the invention when used in the recharge-' able cells produce a considerable improvement in cycle life. The cells employing the present electrolyte (B) without the addition of lead exhibited more than fivefold improvement in cycle life over the standard electrolyte (A) whereas the addition of lead to the present electolyte (C) resulted in nearly a two-fold further improvement, thus demonstrating the effectiveness of these additives.

A further advantage derived from the use of the elecated during charging and particularly on overcharging can be rapidly recombined with the active zinc material without the buildupof dangerous pressure. The anode compact possesses at least about per cent void volume and provides anexcellent semi-wet high surface .area structure for rapid recombination of the oxygen gas evolved. It has been further found that the addition of iin'c oxide to the anode compact aids in maintaining 21 the desirable high concentration of zincate ions at this site during charging and overcharging. Thus the zinc oxide serves as overcharge protection.

What is claimed is:

1. A process for preparing zinc fibers comprising the steps of providing a zinc anode and a cathode in contact with an electrolyte solution comprising a soluble zinc salt and a solvent of high dielectric constant, maintaining the temperature of the electrolyte solution at about 25C., passing an electrical current between said anode and cathode of a magnitude sufficient to provide a cathode current density of at least about 500 amperes per square foot, thereby promoting the electroformation of the zinc fibers at the cathode and then removing the zinc fibers from the cathode.

2. A process for preparing zinc needles comprising the steps of providing a zinc anode and a cathode in contact with an electrolyte solution comprising a soluble zinc salt and a solvent of high dielectric constant, maintaining the temperature of the electrolyte solution above about 25C., passing an electrical current between said anode and cathode of a magnitude sufficient to provide a cathode current density of at least about 500 amperes per square foot, thereby promoting the electroformation of zinc needles at the cathode and then removing the Zinc needles from the cathode.

3. The process in accordance with claim 2 wherein the electrolyte solution is a 47 per cent by weight solu tion of zinc chloride in Water and wherein the tempera ture of the electrolyte solution is maintained above about 80C.

4. The process in accordance with claim 2 wherein the electrolyte solution is a 47 per cent by weight solution of zinc chloride in methanol and wherein the temperature of the electrolyte solution is maintained above about 40C.

5.- A process for preparing zinc filaments comprising the steps of providing a zinc anode and a cathode in contact with an electrolyte solution consisting essentially of a soluble zinc salt selected from the group consisting of the acetate, bromide, chloride, chlorate, formate, iodide, lphenol-4-sulphonate, sulphate, thiocyanate, borate, bromate, fluogallate, fluoborate, fluosili- 22 cate, glycerophosphate, nitrate, phosphate and sulphonate, and a solvent of high dielectric constant, maintaining the temperature of the electrolyte solution at least at about 25C., passing an electrical current be tween said anode and cathode of a magnitude sufficient to provide a cathode current density of at least about 500 amperes per square foot, thereby promoting the electroformation of zinc filaments at the cathode and then removing the electroforrne'd zinc filaments from the cathode.

6. The process in accordance with claim 5 wherein the cathode current densityis maintained above about at least 1000 amperes per square foot.

7. The process in accordance with claim 5 wherein the zinc salt is present in anamount of at least about 30 per cent by weight of the electrolyte solution.

8. The process in accordance with claim 5 wherein the electrolyte solution is a 47 per cent by weight solu tion of zinc chloride dissolved in water.

9. The process in accordance with claim 5 wherein the electrolyte solution is a 47 per cent by weight solution of zinc chloride dissolved in methanol.

10. A process for preparing zinc filaments comprising the steps of providing a zinc anode and a cathode in contact with an electrolyte solution consisting essentially of a soluble zinc salt selected from the group consisting of the acetate, bromide, chloride, chlorate, formate, iodide, l-phenol-4-sulphonate, sulphate thiocyanate, borate, bromate, fluogalla te, fluoborate, fluosilicate, glycerophosphate, nitrate, phosphate and sulphonate and a solvent of high dielectric constant selected from the group consisting of water, alcohols, nitromethane, propylene carbonate and dimethylformamide, maintaining the temperature of the electrolyte solution at least at about 25C., passing an electrical current between said anode and cathode of a magnitude sufficient to provide a cathode current density of at least about 500 thereby amperes per square foot, thereby promoting the electroformation of zinc filaments at the cathode and then removing the electroformed zinc filaments from the cathode.

Claims

1. A PROCESS FOR PREPARING ZINC FIBERS COMPRISING THE STEPS OF PROVIDING A ZINC ANODE AND A CATHODE IN CONTACT WITH AN ELECTROLYTE SOLUTION COMPRISING A SOLUBLE ZINC SALT AND A SOLVENT OF HIGH DIELECTRIC CONSTANT, MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE SOLUTION AT ABOUT 25*C., PASSING AN ELECTRICAL CURRENT BETWEEN SAID ANODE AND CATHODE OF A MAGNITUDE SUFFICIENT TO PROVIDE A CATHODE CURRENT DENSITY OF AT LEAST ABOUT 500 AMPRES PER SQUARE FOOT, THEREBY PROMOTING THE ELECTROFORMATION OF THE ZINC FIBERS AT THHE CATHODE AND THEN REMOVING THE ZINC FIBERS FROM THE CATHODE.

2. A PROCESS FOR PREPARING SINC NEEDLES COMPRISING THE STEPS OF PROVIDING A ZINC ANODE AND A CATHODE IN CONACT WITH AN ELECTROLYTE SOLUTION COMPRISING A SOLUBLE ZINC SALT AND A SOLVENT OF HIGH DIELECTRIC CONSTANT, MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE SOLUTION ABOVE ABOUT 25*C., PASSING AN ELECTRICAL CURRENT BETWEEN SAID ANODE AND CATHODE OF A MAGNITUDE SUFFICIENT TO PROVIDE A CATHODE CURRENT DENSITY OF AT LEAST ABOUT 500 AMPERES PER SQUARE FOOT, THEREBY PROMOTING THE ELECTROFORMATION OF ZINC NEEDLES AT THE CATHODE AND THEN REMOVING THE ZINC NEEDLES FROM THE CATHODE.

3. The process in accordance with claim 2 wherein the electrolyte solution is a 47 per cent by weight solution of zinc chloride in water and wherein the temperature of the electrolyte solution is maintained above about 80*C.

4. The process in accordance with claim 2 wherein the electrolyte solution is a 47 per cent by weight solution of zinc chloride in methanol and wherein the temperature of the electrolyte solution is maintained above about 40*C.

5. A PROCESS FOR PREPARING ZINC FILAMENTS COMPRISING HE STEPS OF PROVIDING A ZINC ANODE AND A CATHODE IN CONTACT WITH AN ELECTROLYTE SOLUTION CONSISTING ESSENTIALLY OF A SOLUBLE ZINC SALT SELECTED FROM THE GROUP CONSISTING OF THE ACETATE, BROMIDE, CHLORIDE, CHLORATE, FORMATE, IODIDE, 1-PHENOL-4-SULPHONATE, SULPHATE, THIOCYANATE, BOATE, BROMATE, FLUOGALLATE, FLUOBORATE, FLUOSILICATE, GLYCEROPHOSPHATE, NITRATE, PHOSPHATE AND SULPHONATE, AND A SOLVENT OF HIGH DIELECTRIC CONSTANT, MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE SOLUTION AT LEAST AT ABOUT 25*C., PASSING AN ELECTRICAL CURRENT BETWEEN SAID ANODE AND CATHODE OF A MAGNITUDE SUFFICIENT TO PROVIDE A CATHODE CURRENT DENSITY OF AT LEAST ABOUT 500 AMPERES PER SQUARE FOOT, THEREBY PROMOTING THE ELECTROFORMATION OF ZINC FILAMENTS AT THE CATHODE AND THEN REMOVING THE ELECTROFORMED ZINC FILAMENTS FROM THE CATHODE.

6. The process in accordance with claim 5 wherein the cathode current density is maintained above about at least 1000 amperes per square foot.

7. The process in accordance with claim 5 wherein the zinc salt is present in an amount of at least about 30 per cent by weight of the electrolyte solution.

8. The process in accordance with claim 5 wherein the electrolyte solution is a 47 per cent by weight solution of zinc chloride dissolved in water.

10. A PROCESS FOR PREPARING ZINC FILAMEOTS COMPRSING THE STEPS OF PROVIDING A ZINC ANODE AND A CATHODE IN CONTACT WITH AN ELCTROLYTE SOLUTION CONSISTING ESSENTIALLY OF A SOLUBLE ZINC SALT SELECTED FROM THE GROUP CONSISTING OF THE ACETATE, BROMIDE, CHLORIDE, CHLORATE, FORMATE, IODIDE, 1-PHENOL-4-SULPHONATE, SULPHATE THIOCYANATE, BORATE, BROMATE, FLUOGALLATE, FLUOBORATE, FLUOSILICATE, GLYCEROPHOSPHATE, NITRATE, PHOSPHATE AND SULPHONATE AND A SOLVENT OF HIGH DIELECTRIC CONSTANT SELECTED FROM THE GROUP CONSISTING OF WATER, ALCOHOLS, NITROMETHAE, PROPYLENE CARBONATE AND DIMETHYLFORMAMIDE, MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE SOLUTION AT LEAST AT ABOUT 25*C., PASSING AN ELECTRICAL CURRENT BETWEEN SAID ANODE AND CATHODE OF A MAGNITUDE SUFFICIENT TO PROVIDE A CATHODE CURRENT DENSITY OF AT LEAST ABOUT 500 THEREBY AMPERED PER SQUARE FOOT, THEREBY PROMOTING ELECTROFORMATION OF ZINC FILAMENTS AT THE CATHODE AND THEN REMOVING THE ELECTROFORMED ZINC FILAMENTS FROM THE CATHODE.