1090880 This invention relates to an alkaline primary battery of the type having a negative electrode containing cadmium or amalgamated zinc and a positive electrode containing monovalent silver oxide, merc~ic oxide, or mixtures of these oxides with manganese dioxide, the positive electrode having an electrochemically active surface area facing the negative electrode. It is a well-known fact that when alkaline primary batteries are stored or used for a very long time, self-discharge phenomena occur which reduce the stored capacity. These self-discharge phenomena are chemical processes which take place at the electrodes as so-called side-reactions. At negative electrodes, the evolution of hydrogen can be such a side-process. It occurs when the potential of the negative electrode is lower (i.e., more negative) than that of a hydrogen electrode in the same electrolyte. It is therefore observed on zinc electrodes, for example, and can be formulated as follows: Zn t H20 -' ZnO ~ H2 The evolution of hydrogen leads to a loss of zinc, i.e., of negative active material. It can be arrested by keeping the hydrogen overvoltage of the zinc electrodes very high, e.g., by carefully excluding contaminants which reduce the overvoltage, or by means of additives to the electrode which increase the overvoltage, e.g., amalgamation. At positive electrodes, self-discharge can be caused by the slubility of the active mater~l. Even when this solubility in the electrolyte is but small, noticeable losses . - 2 - ~, 1090880 of capacity occur in time. Such a loss occurs, for instance, in the case of alkaline primary batteries having positive electrodes which contain monovalent silver oxide or mercuric oxide. In 5M KOH,the solubility of monovalent silver oxide and mercuric oxide is about l~.5 x 10 4 moles of Ag(OH)2 per liter and 3 x 10 moles of Hg(OH)2 per liter, respectively. The dissolved silver oxide or mercu~c oxide diffuses through the separator layer disposed between the electrodes and finally reaches the negative electrode made, for example, of zinc or cadmium. The dissolved silver or mercury oxide is reduced as follows at the negative electrode: Zn + 2 Ag(OH)2 ~ ZnO + 2 Ag + H20 + 2(0H) Zn + Hg(OH)2 ~ . ZnO + Hg~ H20 Cd + 2 Ag(OH)2 ' Cd(OH)2 + 2 Ag + 2(0H) Cd + Hg(OH)2 ~ Cd(OH)2 + Hg Thus at the same time, a corresponding loss of negative active material, zinc or cadmium, occurs. Instead of reacting with the negative electrode, the dissolved silver or mercury oxide may also react with organic substances in the separator system, in which case they are likewise reduced to the corresponding metals. This may give rise to short circuits which drastically accelerate the self-discharge. It is an object of this invention to provide an improved alkaline primary battery designed to reduce this type of self-discharge brought about by the solubllity of the positive active material, without impairing the internal resistance of the battery. To this end, in the alkaline primary battery ~090SS0 according to the present invention, the improvement comprises at least one electrically conductive, microporous, electrolyte- saturated, optically opaque filter-electrode which covers the entire afore-mentioned active surface area of the positive elec- trode, the filter electrode either containing no monovalent silver oxide and no mercuric axide, or containing at most a substantially smaller amount of t~e oxides per unit volume than the positive electrode, the filter electrode containing as principal constituent electrically conducting material which is not corroded, oxidized or dissolved in alkaline electrolytes at the given potential of the positive electrode, and is in electrical contact with the po- sitive electrode. A plurality of filter-electrodes may also be disposed in alternation with separator layers. Several preferred embodiments of the invention will now be described in detail with reference to the accompanying drawing, in whioh: Figure l is a cross-section through an alkaline button cell, a-nd Figures 2-4 are cross-sections through the outer zones of alkaline button cells. ` The invention can also be applied analogously to other geometric configurations. A tablet-shaped positive electrode 2 containing monova- lent silver oxide or mercury oxide is accommodated in a cup 1 made of nickel, nickel-plated sheet steel, or another non-rusting nickel alloy, e.g., according to U.S. Patent No. 3,673,000. The positive electrode 2 is separated from a negative electrode 4, consisting of finely divided amalgamated zinc or finely divided cadmium, by a separator layer 3 of _ - ~.,' . ~90880 polypropylene felt, polyethylene/methacrylic acid polymer, cellophane, cotton, or a similar combination of commercially available separator materials. In the case of a negative electrode 4 of finely divided amalgamated zinc, a cover 5 bears on the inside a layer of copper, bronze, or another amalgamable metal having a high hydrogen overvoltage; the structure of the cover 5 is as described in U.S. Patent No. 3,657,01a. ;- A sealing . ring 6 of nylon, neoprene, or another synthetic material which .10 is not attacked by potassium hydroxide or sodium hydroxide, and which exhibits as- little cold flow as possible, is clamped between the cup 1 and the cover 5, the latter being resiliently .. ,..., I deformed as disclosed in U-S. P.atent No. 3,657,018. A;s. illustrated in Figures 1-4, the galvanic cell according to the lnvention is provided with a metallically . conductive, microporous filter-electrode 7. A rim 8 of this : additional electrode 7 is in electrical contact with the housing cup 1 or with a supporting ring 9 disposed therein for the positive electrode 2. The filter-electrode 7 contains electrically conductive material which, in the electrolyte used and at the given potential of the positive electrode 2, is neither corroded, oxidized, nor dissolved, For alkaline primary batteries containin~ monovalent silver oxide, mercury oxide, or mixtures thereof with manganese dioxide in the positive electrode, substances which. enter into consideration as conducting materi.al for the filter-electrode are graphite, nickel, and certain nickel alloys. (cont'd.) 1090~80 The filter-electrode 7 may also be a porous body made of organic or inorganic materials, the inner surfaces or pore-walls of which are metallized accordingly. Thus the filter-electrode 7 may consist of a metallized felt of synthetic fibers, e.g., nic~el-plated plyester fibers, or it may be a pressed or sintered body of powdered inert metal oxide, e.g., Cd(OH)2, A1203, or ZrO2, the inner pore surface of which is coated with an electrically conductive layer. The filter-electrode 7 may contain not only the aforementioned electrically conductive portion but also other non-conducting or semiconducting, inert fillers which are insoluble in the electrolyte and which affect the pore structure in such a way as to lmpede the diffusion of the monovalent silver oxide or mercury oxide dissolved in the electrolyte. Such additives are, for example, carbon black, manganese dioxide, thermally stabilized or decomposed manganese dioxide, activated carbon, cadmium hydroxide, magnesium oxide, etc. Finally, the filter-electrode 7 may contain binders of an organic or inorganic nature which bind the electrically conductive portions, e.g., polyvinyl pyrrolidone, and also fillers which thicken the electrolyte, e.g., carboxymethyl cellulose. The filter-electrode 7 is from O.l to 2 mm. thick and exhibits a porosity which is--as will be explained in detail below--adapted to the utllization. The porosity may be between 5% and 85% (fraction of the pore volume 0.05 to 0.85) The average pore diameter may be between 0.05 and 50 microns. In any event, the filter-electrode 7 should not - optically exhibit any translucent holes or pores. This clearly 1~9~880 distinguishes the filter-electrode 7 from the structure of an electrically conductive network. The filter-electrode 7 also has a completely different composition, structure, and function than the arrangement for electrodes made of divalent silver oxide described in U.S. Patent No. 3,920,478, which discloses an oxidizable, open screen of a metal such as zinc intended to reduce the potential of the divalent silver oxide electrode. It is the very purpose of this oxidi~able screen that it is supposed to be attacked and thereby reduces the divalent silver oxide. This screen is in no way intended to be a diffusion inhibiting filter. . The same is triue of German Disclosed Application (DOS) No. 2, 525,360 filed on 6 June 1975 and laid open to public inspection on 18 December 1975. It relates to the use of an 15 oxidizable metal such as zinc, cadmium, lead, copper, or silver which is applied to a carrier grid in order to reduce the potential of the divalent silver electrode. It is to be noted in this connection that silver is considered to be oxidizable here because it is exposed to the electric potential 20 of divalent silver oxide. German Disclosed Application (DOS) No. 2, 506,399, filed on 15 February 1975 and laid open to inspection on 26 Augus 1976, likewise relates to a galvanic cell having a positive electrode of divalent silver oxide; the purpose of the arrangemen 25 is to reduce the potential of the electrode to the value of a monovalent silver electrode. This is achieved in that the positive electrode of divalent silver oxide is superficially reduced and insulated from the positive contact can 1 by an electrical~ non-conductive layer of synthetic material, and - 7 - 1090880 the electrical contact to the positive contact can 1 takes place via a porous layer of silver. The porous layer of silver is not inert but oxidizable by the divalent silver oxide, and thus it likewise serves to reduce the potential. It is to be borne in mind in this connection that upon the discharge of silver oxide electrodes, metallic porous layers of silver are formed in any event, whether this is desired or not. In the case of` electrochemical reduction, the porous layer of silver is initially formed chief`ly at the edges of the contact ring. Therefore, the porous layer of silver formed does not serve the purpose of a non-oxidizable, diffusion-inhibiting filter-electrode which remains stable during a long period of storage, in the sense of the present invention. The essential features of the present invention are that the filter-electrode does not contain any proportion (or at most only a substantially reduced proportion) of monovalent silver oxide or mercury oxide, that it is electrically conductive, that under the given conditions of electrolyte composition and potential it is not chemically or electrochemica~ attacked, oxidized, or dissolved, and that it covers the entire free surface area of the positive electrode facing the negative electrode. The invention also comprises an arrangement in which an additional separator layer is inserted between the filter-electrode 7 and the positive electrode 2. The additional separator layer of organic or inorganic material should be permeable to OH ions but should retard the diffusion of dis- solved monovalent silver oxide or mercury oxide into the f'ilter~electrode. The additional separator layer may consist 1090880 of oxidation-resistant, commercially available separator ma- terial, e.g., of polypropylene felt and methacrylic acid/poly- ethylene polymer, etc. The following examples set forth the manner in which the filter-electrode may be produced. The examples relate to an alkaline mercury oxide/cadmium button cell 17.4 mm. in diameter and 7.5 mm. high. The positive electrode consisted ¦ of mercury oxide with an admixture of 5% powdered graphite l and 9~ manganese dioxide. The negative electrode consisted of 10 ¦ sponge cadmium, the separators of the commercially available combination specified below. Example 1 A nickel wire netting having a mesh size of l 0 4 mm. and a wire gauge of 0.1 mm. was lmmer~d in a viscous 15¦ paste of carbonyl-nickel powder, average grain size 2.6 to 3.4 microns, water, and a thickening agent such as gelatine, methyl cellulose, starch, etc., then dried and sin~ered at 900C for 15 minutes. The result was a highly porous (degree of porosity 0.85) sinter nickel plate 0.4 mm. thick, out of which discs 16 mm. in diameter were punched. The discs were pressed into the supporting ring 9 as filter-electrodes 7, as -shown in Figure 1, whereupon the rim portion 8 was compressed. The tablet 2 of mercuric oxide was then laid in place, and the entire assembly was pressed into the cup 1. The commercially available, mlcroporous separators of syntheticnonwoven fabrik, polyethylene/methacrylic acid polymer, cellulose, and cotton were laid upon the sintered, porous filter-electrode 7. A plastic washer 10 of the synthetic resin polymer product sold under the registered trademark "Te~lon" covered the peripheral ~090880 portion of the filter-electrode 7. The cell was discharged at 75C across resistances of` 1200 ohms. It was found that the separators were far less oxidized and that less dissolved mercury oxide diffused to the negative electrode than in cells without a filter-electrode. Example 2 A mixture of 99% finely divided graphite and 1% polyvinyl pyrrolidone as binder was pressed into a tablet 13 mm. in diameter and 0.4 mm. thick and inserted into a cell as the filter-electrode j, as shown in Figure 2. The filter- electrode 7 was in mechanical and electrical contact with the inner rim 9a of the supporting ring 9. As in Example 1, the separator layers 3 were disposed over the filter-electrode 7. Here again, after discharge at a high temperature (75C), it 15 ¦ was found that the separators were practically not attacked. No trace of metallic mercury was found on the negative elec- trode. The filter-electrode had prevented the diffusion of dissolved mercury oxide. Example 3 A mi~ture of 50% finely divided graphite, 49 manganese dioxide which had previously been stabilized for 4 hours at 400C, and 1% polyvin~l pyrrolidone as binder was pressed into a tablet and disposed as shown in Figure 3. The manganese dioxide brought about a very fine-pored structure of the filter-electrode, which became very well wetted with alkaline electrolyte. Af'ter discharge at 75C, metallic mercury was to be found neither on the separator layers nor in the cadmium electrode. 090880 Example_4 ~ s illustrated in Figure 4, a further separator layer ll of electrically non-conductive material was inserted here between the filter-electrode 7 and the positive electrode 2. It consisted of a polypropylene felt lying upon the positive electrode and a diaphragm made of polyethylene/methacrylic acid polymer, which is sold under the trade mark "Permion". The purpose of the additional separator layer 11 between the filter-electrode 7 and the positive electrode 2 was to impede still further the diffusion o-f mercury oxide dissolved in the electrolyte. The composition of the filter-electrode was 50~ powdered graphite, 4~.5~ manganese ~dioxide, 1% polyvlnyl pyrrolidone, and 0.5~ carboxymethyl cellulose as a thickenin.g agent for the alkali electrolyte. After discharge at 75C, no mercury was detected on the surface of the filter- electrode facing the negative electrode. . The~ foregoing examples show that with the aid of the filter-electrode described, it is possible largely to prevent the diffusion of dissolved positive, active material to the negative electrode and to the. separator layers. Thus both the earlier- . mentioned loss of negative active material and the destructionof the separators by oxidation can be avoided. Such filters are advantageous in MgO-Cd, HgO-Zn.Ag2O-Cd, and Ag2O-Zn cells. - The mode of operation of the additional filter-electrode may be physically described in the following manner. During discharge, the current distribution in the positive electrode adjusts itsel. in such a way that first that ._ . , ~ . = --11-- B 109~1~80 material to which the least electrical resistance leads is reduced. The electrical resis~nce is composed of the resistance of the ion flow in the electrolyte and the resist~nce of the electron flow in the electrically conductive portion of the positive electrode. By introducing the metallically conductive filter-electrode between the positive and negative electrodes, preferably that positive active material is first reduced which di~fuses into the filter-electrode since the ohmic voltage drop to this reaction location is the smallest. Based upon the example of a mercury oxide positive electrode and a 5M KOH electrolyte, it shall now be shown how the filter-electrode can be dimensioned so that no dissolved mercury oxide reaches the negative electrode. The amount(m)of dissolved mercury oxide, Hg(OH)2, diffusing into the filter-electrode per unit of time is roughly approximated by m = D (dc/dx) p (1/t) r ~ and the corresponding reduction current which is needed to re- duce this number of moles of Hg(OH)2 per second in the filter- electrode is approximately - i = 2F D ( a c/ a x) p (1/t) r2 ~ wherein F = 96500 coulombs, D is the coefficient of diffusion (cm /sec.) of dissolved Hg(OH)2, a c/ a x is the linearized gradient of concentration in (moles/cm3)/cm., p is the porosity (fraction of the pore ~olume), t is a tortuosity coefficient of the porous filter-electrode, and r is the radius of the filter- electrode. If D = lO 5 cm3/sec., a c - 3 x. lO 7 moles/cm3, ~ x = O.l cm., p = 0.5, (1/t) = 0.2, and r = 0.65, the result is a reduction current of Ç~ 8 x lO 7 amps. If the battery is ~0908~ constantly loaded with currents above this limit, then theo- retically, according to this simplified calculation, no dis- solved mercury oxide would reach the negative electrode or the separator, and the solubility of the mercury oxide contained in the positive electrode could not cause any loss of capacity at all. By taking into consideration the electrolyte resistance in the pores of the filter-electrode, as well as the velocity of the electrochemical reaction Hg(OH)2 ~ 2 ~ ~_ Hg ~ 2(0H) as a function of the local potential in the filter-electrode, which potential is determined by the ohmic voltage drop in the electrolyte-filled pores, differential equations could be set up by means of which a more exact current distribution in the filter-electrode would be computable. However, even the ap- proximate calculation shows that the filter-electrode effectively reduces the self-discharge when batteries are loaded with low currents over a long period of use. The smaller the pore diameter and the less the porosity, the more effective the filter-electrode. The electrolyte resistance in the pores thereby increases, and the reduction takes place at a lower potential to an even greater extent in the f'ilter-electrode. A higher internal resistance of the cell must naturally then be tolerated. In the dimensioning of the filter-electrode, it must also be taken into account that the reduction of dissolved oxide brings about a depositiori of metal which may reduce the porosity. In such cases, it may be advantageous not to bind the particles of the filter-electrode rigidly but rather 109088() to dispose them in the form of a more or less movable or flexible bed. The porosity should initially be great enough to allow for this factor. In the case of open circuit storage, too, the filter-electrode aids in lessening the diffusion of dissolved monovalent silver oxide or mercury oxide s-ince the concentration gradient must develop over a longer distance, and the rate of diffusion is slowed by the described measures in the filter- electrode. The hydrogen produced by the self-discharge of negative zinc electrodes can diffuse to the filter-electrode and there serve as an electrochemical reducing agent for the dis- solved monovalent si~ver oxide or the dissolved mercury oxide. Organic components of the separator may also dissolve in traces in the electrolyte and penetrate into the filter-electrode, where they may serve as reducing agents for the dissolved silver or mercury oxides. These side-reactions can contribute to ensuring that during open circuit storage, less dissolved silver oxide or mercury oxide reaches the negative electrode, where it would cause the aformentioned self-discharge. (cont'd.)