HK1007407A1 - Alkaline cell having a cathode including an additive - Google Patents

Alkaline cell having a cathode including an additive Download PDF

Info

Publication number
HK1007407A1
HK1007407A1 HK98106310A HK98106310A HK1007407A1 HK 1007407 A1 HK1007407 A1 HK 1007407A1 HK 98106310 A HK98106310 A HK 98106310A HK 98106310 A HK98106310 A HK 98106310A HK 1007407 A1 HK1007407 A1 HK 1007407A1
Authority
HK
Hong Kong
Prior art keywords
additive
cathode
cell
weight percent
cells
Prior art date
Application number
HK98106310A
Other languages
German (de)
French (fr)
Chinese (zh)
Other versions
HK1007407B (en
Inventor
M. Swierbut Wendi
C. Nardi John
Original Assignee
Eveready Battery Company, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Eveready Battery Company, Inc. filed Critical Eveready Battery Company, Inc.
Publication of HK1007407A1 publication Critical patent/HK1007407A1/en
Publication of HK1007407B publication Critical patent/HK1007407B/en

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/06Electrodes for primary cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0002Aqueous electrolytes
    • H01M2300/0014Alkaline electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/04Cells with aqueous electrolyte
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Primary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Hybrid Cells (AREA)

Abstract

The cell has an cathode comprising a manganese dioxide active material and an additive comprising a titanate. The additive constitutes between about 0.1 to 10 weight percent of the cathode. The cathode pref. comprises a manganese dioxide active material and an additive comprising BaTiO3. The cathode may comprise a manganese dioxide active material and an additive comprising K2TiO3.

Description

The present invention generally relates to electrochemical cells including cathode additives and more particularly to primary alkaline electrochemical cells having cathodes formed of manganese dioxide, one or more titanate additives, and other cathode components.
US-A-4,465,747 discloses various additives, including titanates such as Li2TiO3, for non-aqueous cells to suppress build-up of internal impedance in the cell during storage or discharge. These additives may be incorporated as additional additives in the cathodes of the non-aqueous cells disclosed in US-A-4,478,921, which contain manganese carbonate as the primary additive to improve the pulse voltage capability of the cell at low temperatures.
A typical alkaline cell would comprise: a steel cylindrical can having a cathode comprising manganese dioxide as the active material, generally formed on the interior surface of the steel can; an anode comprising zinc, generally located in the centre of the cell; a separator located between the anode and the cathode; and an alkaline electrolyte simultaneously contacting the anode, cathode, and separator. A conductive anode current collector is inserted into the anode active material and a seal assembly closes the open end of the steel can.
A primary goal in designing alkaline batteries is to increase the service performance of the cell. The service performance is the length of time for the cell to discharge under a given load to a specific voltage at which the cell is no longer useful for its intended purpose. One approach taken to increase service performance was to increase the interior volume of the cell in order to increase the amount of active materials within the cell. However, the commercial external size of the cell is fixed, thereby limiting the ability to increase the amounts of active materials within the cell. In order to accommodate more active materials within the cell while maintaining the external size of the cell, the steel label of the conventional alkaline cell has been replaced with one made of thinner metalized plastic film. Thus, the steel can may be enlarged to provide a greater internal volume. By switching to a thinner plastic film label, the service performance of a typical alkaline cell was significantly increased.
Another approach taken to increase the service performance of a cell is to utilize an anatase titanium dioxide as an additive to a cathode having manganese dioxide as the active material.
Despite past increases in service performance, the need to find new ways to increase service performance remains the primary goal of cell designers.
WO-A-9708770 (filed on 29 March 1996 and published on 6 March 1997) discloses various additives, including BaTiO3 and MgTiO3, for alkaline cells to increase the service life of the cell. This reference is not relevant to the present application to the extent that this application is entitled to its claimed priority date.
The present invention improves the service performance of alkaline cells by the addition of one or more titanate additives to the active cathode material. Thus, the present invention provides an aqueous alkaline electrochemical cell having an anode, a cathode, and an electrolyte, said cathode comprising a manganese dioxide active material and an additive, wherein the additive comprises a titanate.
The titanate additive is preferably one or both of BaTiO3 or K2TiO3.
The cathode of the present invention is particularly adapted for use in an electrochemical cell having a zinc anode and an alkaline electrolyte.
In a preferred embodiment, the titanate additive constitutes from 0.1 to 10 weight percent of said cathode, preferably from 1 to 5 weight percent of said cathode and, when the additive is K2TiO3, preferably from 1 to 2 weight percent of said cathode.
The invention is further illustrated by reference to the accompanying drawings, in which:
  • Figure 1 is a cutaway perspective view of an example of an electrochemical cell constructed in accordance with the present invention; and
  • Figure 2 is a comparative graph of the service performance of a standard alkaline cell having a cathode with no additives and electrochemical cells having cathodes with additives in accordance with the present invention.
Figure 1 shows a cutaway view of a typical cylindrical alkaline battery 10. Alkaline battery 10 includes a steel can 15 having a cylindrical shape and one open end. A metalized, plastic film label 16 is formed about the exterior surface of steel can 15 except for the ends of steel can 15. At the closed end of steel can 15 is a positive cover 17 preferably formed of plated steel. Film label 16 is formed over the peripheral edge of positive cover 17.
In the embodiment shown, a cathode 20 preferably formed of a mixture of manganese dioxide, graphite, 45% potassium hydroxide solution, deionized water, an aqueous TEFLON™ solution of 20% polytetrafluoroethylene, and an additive, is formed about the interior side surface of steel can 15. A separator 30, which is preferably formed of a non-woven fabric that prevents migration of any solid particles in the battery, is disposed about the interior surface of cathode 20. An electrolyte 40 formed of potassium hydroxide is disposed in the interior of separator 30. An anode 50, preferably formed of zinc powder, a gelling agent and other additives, is disposed within electrolyte 40 in contact with a current collector 60, which may be formed of brass.
Current collector 60 contacts a brass rivet 70 formed at the open end of steel can 15. A nylon seal 71 is formed at the open end of steel can 15 to prevent leakage of the active ingredients contained in steel can 15. Nylon seal 71 contacts a metal washer 72 and an inner cell cover 74, which is preferably formed of steel. A negative cover 75, which is preferably formed of plated steel is disposed in contact with inner cell cover 74 and brass rivet 70, which contacts current collector 60 through a hole formed in nylon seal 71. Negative cover 75 is electrically insulated from steel can 15 by nylon seal 71.
The cathode of the present invention for a D-size cell is preferably composed of approximately 71.7 to 81.7 weight percent MnO2, about 8.5 weight percent graphite, about 7.9 weight percent of an alkaline solution, such as an aqueous 45% KOH solution, about 0.4 weight percent deionized water, about 1.5 weight percent binder material, such as an aqueous TEFLON™ solution of 20% polytetrafluoroethylene, and approximately 0.1 to 10 weight percent of an additive. More preferably, the weight percent of MnO2 is between about 76.8 and 80.8 and the weight percent of the additive is between 1 and 5 such that the combined weight percent of MnO2 and the additive is a constant of preferably approximately 81.8. The amount of alkaline solution used in the cathode varies according to cell size as does the amount of the binder material. The additive is a titanate, preferably BaTiO3 or K2TiO3.
The cathode may be made by weighing out the needed materials and mixing the MnO2, the titanate additive, and the graphite and blending to obtain a homogeneous mixture. The deionized water, the TEFLON™ solution, and the KOH solution are then mixed with the dry cathode components to form a homogeneous cathode mix. The cathode mixture is then placed in steel can 15 and moulded into an annular, cylindrical shape.
As stated above, it has been discovered that the addition of small amounts of the above listed additives significantly increases the service performance of alkaline electrochemical cells. The following example illustrates the advantages obtained from practicing the present invention.
EXAMPLE
Control alkaline D-size cells were prepared as described above except that no additive was included in the cathodes. Thus, the composition of the cathode in the cell of the present invention was approximately 80.16 weight percent MnO2, about 1.6 weight percent titanate, about 8.52 weight percent graphite, about 7.87 weight percent of a 45% aqueous solution of potassium hydroxide (KOH), about 0.36 weight percent deionized water, and about 1.49 weight percent of a TEFLON™ binder solution. In the control cell, the weight percentage of MnO2 relative to the cathode was equal to the combined weight percentage of MnO2 and the additive in the experimental cells. Experimental D-size cells having a BaTiO3 additive and other experimental D-size cells having a K2TiO3 additive were constructed, along with control cells having no additive. Each cell was connected to a 2.2 Ohm load for one hour per day. Figure 2 shows the resulting time versus voltage discharge profiles for the cells. For a 1.00 volt cutoff, the experimental cells with the K2TiO3 additive showed an average 10% increase over the service performance of the control cell and the experimental cells having the BaTiO3 additive exhibited an average 8% increase in service performance over the control cells. At a 0.80 volt cutoff, the experimental cells having the K2TiO3 additive had an average 13% increase-in service performance over the control cells, while the experimental cells having the BaTiO3 additive had an average 10% increase in service performance over the control cells.
As is apparent from the above example, significant increases in service performance of an alkaline electrochemical cell may be obtained using additives of BaTiO3 and K2TiO3.
Although the above example used D-size cells, it will be appreciated by those skilled in the art that the increase in service performance may be obtained regardless of the cell size. Because some of the above additives perform better than others in continuous tests while others perform better in intermittent tests, it may be desirable to combine such additives to enhance the overall service performance of an electrochemical cell for both continuous and intermittent use.

Claims (7)

  1. An aqueous alkaline electrochemical cell having an anode, a cathode, and an electrolyte, said cathode comprising a manganese dioxide active material and an additive, characterised in that the additive comprises a titanate.
  2. An electrochemical cell according to claim 1, wherein said anode includes zinc.
  3. An electrochemical cell according to claim 1, wherein said additive constitutes from 0.1 to 10 weight percent of said cathode.
  4. An electrochemical cell according to claim 3, in which said additive constitutes from 1 to 5 weight percent of said cathode.
  5. An electrochemical cell according to any one of claims 1 to 4, in which the additive is BaTiO3.
  6. An electrochemical cell according to any one of claims 1 to 4, in which the additive is K2TiO3.
  7. An electrochemical cell according to claim 6, in which said additive constitutes from 1 to 2 weight percent of said cathode.
HK98106310.3A 1995-06-07 1998-06-24 Alkaline cell having a cathode including an additive HK1007407B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US479591 1995-06-07
US08/479,591 US5569564A (en) 1995-06-07 1995-06-07 Alkaline cell having a cathode including a titanate additive

Publications (2)

Publication Number Publication Date
HK1007407A1 true HK1007407A1 (en) 1999-04-09
HK1007407B HK1007407B (en) 2000-09-29

Family

ID=

Also Published As

Publication number Publication date
SG72693A1 (en) 2000-05-23
DE69603670T2 (en) 2000-03-23
CN1146640A (en) 1997-04-02
TW409437B (en) 2000-10-21
EP0747980A1 (en) 1996-12-11
JP4015211B2 (en) 2007-11-28
EP0747980B1 (en) 1999-08-11
CA2178422A1 (en) 1996-12-08
KR970004129A (en) 1997-01-29
JPH09139201A (en) 1997-05-27
US5569564A (en) 1996-10-29
DE69603670D1 (en) 1999-09-16

Similar Documents

Publication Publication Date Title
EP0747980B1 (en) Alkaline cell having a cathode including an additive
US5501924A (en) Alkaline cell having a cathode including a tin dioxide additive
EP0747982B1 (en) Cathodes for electrochemical cells having additives
AU674090B2 (en) Additives for primary electrochemical cells having manganese dioxide cathodes
US20020068220A1 (en) Electrochemical cell and negative electrode therefor
EP1473788A1 (en) Alkali cell
JP2001015106A (en) Alkaline battery
EP1203417B1 (en) Alkaline cell with improved anode
EP0617845B1 (en) Cathodes for zinc manganese dioxide cells having barium additives
US5895734A (en) Alkaline cell having a cathode including a titanate additive
US6203943B1 (en) Electrochemical cell having electrode additives
CA2351089A1 (en) Electrochemical cell having electrode additives
EP1293002B1 (en) Electrochemical cells with an anode containing sulfur
JP2000048827A (en) Alkaline battery
HK1007407B (en) Alkaline cell having a cathode including an additive
JPH10189006A (en) Air cell
HK1007406B (en) Alkaline cell having a cathode including an additive
HK1007408B (en) Cathodes for electrochemical cells having additives
HK1068029B (en) Alkaline battery

Legal Events

Date Code Title Description
PF Patent in force
PC Patent ceased (i.e. patent has lapsed due to the failure to pay the renewal fee)

Effective date: 20100607