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Publication numberUS3066179 A
Publication typeGrant
Publication dateNov 27, 1962
Filing dateApr 28, 1961
Priority dateApr 28, 1961
Also published asDE1421582A1, DE1421582B2
Publication numberUS 3066179 A, US 3066179A, US-A-3066179, US3066179 A, US3066179A
InventorsRuben Samuel
Original AssigneeRuben Samuel
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Electric current producing cell
US 3066179 A
Abstract  available in
Images(2)
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Claims  available in
Description  (OCR text may contain errors)

N0V 27, 1962 s. RUBEN 3,066,179

ELECTRIC CURRENT PRODUCING CELL iled April 28, 1961 2 Sheets-.Sheet 1 R. ww L F. M 5

www C M ATTORNEYS Nov. 27, 1962 s. RUBEN ELECTRIC CURRENT PRODUCING CELL 2 Sheets-Sheet 2 Filed April 28, 1961 wk ,8x6 .gew .Si wss N o. w f M M u n H/ H 9v N .Wm W M/ M M W M/ M QQ. MM M/ u. M/ M QR m M n HV ww @m W W QN Qm il@ W I mK SSR l Si MQMRNR SSS Arianne-YS United States Patent 3,066,179 ELECTRIC CURRENT PRODUCING CELL Samuel Ruben, 52 Seacord Road, New Rochelle, N .Y. Filed Apr. 28, 1961, Ser. No. 106,231 11 Claims. (Cl. 13G-83) This invention relates to an alkaline primary cell, more specifically to such a cell using a depolarizing oxide mixed with carbon or graphite in contact with a steel container as the cathode thereof.

For many applications, such as power sources for ash bulbs, it is very important to obtain the maximum possible flash current. This is particularly true in a situation such as indicated above where, if the current is insuicient, the bulb will not fire In order to accomplish this, it is necessary to obtain the minimum contact resistance between the cathode depolarizer and the cathode container.

An additional problem which presents itself is 4that the cell may have a satisfactory iiash current initially, but later, after some storage, the current falls below an acceptable level.

This is due primarily to relaxation of the depolarizer mix density which results from penetration of the mix by the electrolyte. This increases the voltage drop or contact resistance across the depolarizer-steel (or nickel plated steel) cathode container and hence reduces the ash current. An additional factor in the MnOZ cell is the increase of the MnOZ-Ni plate contact resistance due to oxidation even when silver plate is used. Some of the synthetic MnO2 ores have a slight sulfide contact potential with silver sulides and this causes an increase in contact resistance over a period of time. However, gold is inert and, when a gold plate is used not only is a low contact resistance maintained, but the flash current may actually increase.

Unlike the zinc-AgO cell described in applicants prior United States Patent No. 2,542,710, depolarizing oxides such as MnOz do not reduce to a metal. The cell reaction yields Mn2O3 which has an even higher potential drop at the cathode can interface than does MnO2. Therefore, as can readily be seen, as the cell is used, the potential drop increases and the ash current decreases.

Therefore, it is among the objects of this invention to provide a cell with a maximum iiash current.

It is also among the objects of this invention to provide a cell which has a minimum contact resistance between the depolarizer and the steel cathode container.

It is further among the objects of this invention -to provide a cell which not only maintains a maximum iiash current on storage but in which the ash current actually increases with the passage of time.

It is still further among the objects of this invention -to provide a cell which will retain' the minimum contact resistance between the cathode and the container during use.

It is still further among the objects of this invention to provide a cell wherein the tiash current is increased up to 25% over corresponding cells without the present invention.

It is still further among the objects of this invention to provide a cell which will maintain a low contact resistance on storage.

In practicing the present invention, there is provided, for example, an alkaline primary cell having an amalgamated Zinc anode, a cathode composed of a mixture of 91% MnO2 and 9% micronized graphite, and a steel or nickel plated steel container. A spacer-barrier is placed between the anode and the cathode both to prevent direct contact between the anode and cathode as Well as to absorb and retain substantial quantities of electrolyte. The electrolyte is in the form of a potassium zincated water solution of KOH; and there is a thin plate of a low resist- 3,066,179 4Patented Nov'. 27, 1962 "ice ance and gold on the container and in contact with the cathode.

The cathode depolarizer is made by mixing 91% of synthetic MnO2 with 9% of micronized graphite and pressing said mixture into cylindrical pellets which are then forced into the steel cathode container having a gold plate on its inner surface.

The spacer-barrier is composed of spirally wound cellulose with an outer wrapping of parchment. This spacerbarrier is placed inside the cylindrical depolarizer pellets. Cylindrical pellets of amalgamated zinc containing about 13% mercury are placed inside of the central opening in the spacer-barrier. These pellets are formed by pressing the powdered zinc. The pellets rest on a neoprene block or pressure pad which prevents contact with the bottom of the cathode container.

The electrolyte is added by injection into the opening in the center of the anode cylinders and passes into the spacer-barrier which absorbs it. This causes the spacer to swell, filling the space between the anode and the cathode, and thus insuring good electrolytic contact between those elements.

The inner and outer caps are applied with an insulating grommet and the outer can is crimped against the grommet. This seals the cell and presses the anode pellet against the compressible neoprene pad which insures maintenance of good contact with the caps.

In the accompanying drawing constituting a part hereof and in which like reference characters indicate like parts,

FIG. 1 is an elevation partly in section, showing a cell according to the present invention; and

FIG. 2 is a chart comparing the flash currents of cells having gold and silver inner can platings, over a period of six months.

The cell 1 is composed of an outer can 2, a cathode co-ntainer 3, a cathode in the form of cylnidrical pellets 4, and an anode of cylindrical amalgamated zinc pellets 6. A spacer-barrier 5 is between the anode and cathode and absorbent sleeve 7 is placed between outer can 2 and cathode container 3. Plastic grommet 8 insulates can 2 and container 3 from contact with inner cap 9 and outer cap 10. The double cap arrangement prevents leakage and creepage of electrolyte outside the cell.

Beneath the zinc pellets 6 is placed pressure pad 12 which insulates the pellets from contact with the container 3 and also, `due to its resiliency, urges the pellets 6 upward against inner cap 9. This achieves excellent contact btween the anode and the terminal caps. On outer cap 10 is anode contact 11 for aiding in obtaining good external contact.

Gold plate 13 is deposited on container 3 by electroplating or galvanic contact plating so that good contact is made between cathode 4 and container 3. This reduces the contact resistance and increases the flash current by as much as 25%.

In FIG. 2, there is presented the results of tiash current tests made on cells of the contsruction shown in FIG. l, using a depolarizer consisting preponderately of MnO2, an amalgamated zinc anode and an alkaline zincated electrolyte.

The cells were identical except that the steel depolarizer containers were silver plated in one case and gold plated in the other. One hundred cells of each type were stored and read at room temperature. The readings in each group were averaged and plotted on FIG. 2.

While only one specific embodiment of this invention has been described, such changes as would be obvious to one skilled in the art may be made Without departing therefrom. For example, substantial changes in the shape and formation of the various elements of the cell may be made, so long as the cathode container is plated with gold.

The teachings of the present invention are applicable to 3 similar .cells .in .which the Vdepolarizer is .preponderately HgO with generally similar results.

These and similar changes may be made without departingfrornthescope and spiritof this invention, which is to be broadly construed and not to be limited except by the character of the claims appended hereto.

i claim:

l. A primary cell comprising a steel container, a lining of gold on at least the inner surface of said container, a cathode depolarizer consisting preponderately of a material taken Vfrom `the .class consisting Vof MnOZ kand HgO /closelyiitting in said container and in `contact with said lining, an electrolyte, an anode and an electrolyte absorb- "ent Vspacer between Vsaid cathode and anode.v

.2. .-A cell according to claim V1 wherein said material I'S rNIHOZ.

3. lAcell according to claim 1 wherein said material is HgO.

4. A cell according to claim .1 wherein said cathode includes Va relatively fsmall proportion of carbon.

5. .A cell laccording to claim l wherein .the electrolyte consists of an aqueous zincated solution of KOH.

6. A primary cell comprising an vamalgamated zinc anode, a cathode `composed of Va mixture of graphite and arcompound taken from the class Vconsisting of MnO2 .and HgO, a steel ycontainer housing said cathode, a spacer between said anode vand said cathode, an electrolyte consisting ofpotassium zincated KOH and water, and a vthin plate of gold on said container and in contact with said cathode.

7. A cell according to claim 6 in which said compound l5 M1102.

8. A cell according to claim 6in which said compound is H'gO.

9. An electric current producing cell comprising a steel container, a gold plate on the inside surface thereof, a cathode composed of a mixture oftgraphite and a compound taken from the class consisting of Mn02 and HgO ,in intimate contact With said plated surface, an anode and an electrolyte.

10. An electric current producing cell comprising a metal member, a gold plate on the surface of said member, an oxygen yielding depolarizer consisting preponderately of a material taken -from the class consisting of M1102 and Hg() in intimate contact with said plated surface, an anode and an electrolyte.

ll. A cell according to claim l0 wherein said member issteel.

References Cited inthe leof this patent UNITED STATES PATENTS 25 2,650,945 Herbert Sept. l, 1953 2,705,249 :Ellis Mar. 29, 1955 2,902,530 'Eisen Sept. l, 1959

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2650945 *Jul 8, 1949Sep 1, 1953Ray O Vac CoPrimary dry cell
US2705249 *Sep 5, 1950Mar 29, 1955Grenville B EllisPrimary alkaline cell
US2902530 *Oct 12, 1955Sep 1, 1959Bjorksten Res Lab IncBattery constituents
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3485675 *Jun 6, 1967Dec 23, 1969Samuel RubenElectric current producing cell having depolarizer in intimate contact with carburized surface of the container
US3630783 *May 11, 1970Dec 28, 1971Mallory Battery CanadaHeat-shrinkable packaging for batteries
US4663248 *Sep 7, 1982May 5, 1987Duracell Inc.Electrode terminal contact
US5447809 *Nov 3, 1994Sep 5, 1995Rayovac CorporationAlkaline primary battery containing coated current collector
US5814419 *Sep 1, 1995Sep 29, 1998Rayovac CorporationAlkaline manganese dioxide electrochemical cell having coated can treated with sodium silicate
US6153330 *Jul 31, 1998Nov 28, 2000Rayovac CorporationAlkaline manganese dioxide electrochemical cell having coated can treated with silicon compounds
US6258132Apr 27, 1999Jul 10, 2001Eveready Battery Company, Inc.Process for producing in an alkaline cell an in situ silver layer on a cathode container
EP1040529A1 *Oct 15, 1998Oct 4, 2000Avista LabsA proton exchange membrane fuel cell power system
WO2000065673A1 *Apr 25, 2000Nov 2, 2000Eveready Battery IncAlkaline cells having a conductive metal layer on a cathode container and process for making such
Classifications
U.S. Classification429/164, 429/133, 429/224, 429/169
International ClassificationH01M6/06, H01M4/66
Cooperative ClassificationY02E60/12, H01M4/661, H01M4/669, H01M6/06
European ClassificationH01M6/06, H01M4/66A, H01M4/66S