US20030113623A1 - Oxazoline surfactant anode additive for alkaline electrochemical cells - Google Patents

Oxazoline surfactant anode additive for alkaline electrochemical cells Download PDF

Info

Publication number
US20030113623A1
US20030113623A1 US10/020,685 US2068501A US2003113623A1 US 20030113623 A1 US20030113623 A1 US 20030113623A1 US 2068501 A US2068501 A US 2068501A US 2003113623 A1 US2003113623 A1 US 2003113623A1
Authority
US
United States
Prior art keywords
anode
surfactant
oxazoline
alkaline
cells
Prior art date
Legal status (The legal status 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 status listed.)
Abandoned
Application number
US10/020,685
Inventor
Ernest Ndzebet
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Spectrum Brands Inc
Original Assignee
Rayovac Corp
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 Rayovac Corp filed Critical Rayovac Corp
Priority to US10/020,685 priority Critical patent/US20030113623A1/en
Assigned to RAYOVAC CORPORATION reassignment RAYOVAC CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: NDZEBET, ERNEST
Priority to AT02797314T priority patent/ATE556445T1/en
Priority to EP02797314A priority patent/EP1506584B1/en
Priority to AU2002361674A priority patent/AU2002361674A1/en
Priority to PCT/US2002/039990 priority patent/WO2003052843A2/en
Publication of US20030113623A1 publication Critical patent/US20030113623A1/en
Assigned to ROVCAL, INC. reassignment ROVCAL, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: RAYOVAC CORPORATION
Priority to US10/944,036 priority patent/US6927000B2/en
Abandoned legal-status Critical Current

Links

Images

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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • 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
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/04Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
    • H01M12/06Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
    • 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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • 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
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/42Alloys based on zinc

Definitions

  • Metal air cells contain an anode and an oxygen cathode, with the oxygen usually obtained from ambient air.
  • the oxygen cathode catalytically promotes the reaction of oxygen with an aqueous neutral or alkaline electrolyte and is not consumed or changed during discharge.
  • the cathode is extremely compact yet has essentially unlimited capacity, very high energy densities are achieved, resulting from the increased available volume for the anode active material.
  • a metal-air cell can provide more watt-hours of electromotive force than a so-called “two-electrode cell” of similar cell size, mass and anode composition that contains both anode- and cathode-active materials inside the cell structure.
  • Metal-air cells have an advantageous watt-hour capacity/mass ratio without regard to size or configuration, which can be, e.g., button cells as in, for example, U.S. Pat. No. 5,721,065 (“the '065 patent”), or cylindrical cells as in, for example, U.S. Pat. No. 6,210,827 (the '827 patent”), each incorporated by reference in its entirety as if set forth herein.
  • a typical metal air cell such as a zinc air cell contains an anode that includes a zinc alloy powder, a carbon-based air cathode and an alkaline electrolyte with a gelling agent to prevent the electrolyte from creeping through the cell seals.
  • the anode of a zinc air cell should participate only during current-generating reaction periods.
  • corrosive shelf-discharge side reactions in the alkaline electrolyte can reduce both service and shelf life of alkaline electrochemical systems that use zinc as the anode active material.
  • Much effort has been directed to improving electrochemical reaction efficiency and cell output.
  • mercury was added to cell anodes to improve corrosion resistance. In recent years, mercury has been replaced by substances that conform to environmental requirements.
  • the '065 patent discloses a button cell having an anode mix containing zinc metal powder, indium or other compounds, optionally a low level of mercury, a gelling agent and preferably a hydroxyethylcellulose surfactant.
  • the anode disclosed therein sustains longer periods of power production at a relative steady voltage of at least 1.1 volts while protecting the anode metal from corrosion in the alkaline environment.
  • the '827 patent discloses a cylindrical cell having an anode mix containing electrolyte, a gelling agent, particulate zinc, zinc oxide, additives and an organic surfactant comprising hydroxyethylcellulose.
  • Japanese Patent No. JP10083812 to Toshiba Battery Co. Ltd. discloses providing a high performance zinc alkaline battery containing 0.5-100 ppm of a fluorine-containing surfactant in a non-amalgamated-zinc-alloy-based gelled anode having a viscosity of 100,000 to 300,000 cPs at 25° C.
  • U.S. Pat. No. 5,382,482 concerns suppressing dendrites and shape change in an alkaline cell by disposing a cross-linked polymer film layer in close proximity to the anode active material, where the polymer film layer can contain, among other polymers, polyoxazoline.
  • the patent does not describe including an oxazoline surfactant in the anode mix of the cell.
  • an alkaline electrochemical cell having superior discharge performance and corrosion resistance includes an oxazoline surfactant additive in the cell anode.
  • the present invention relates to an anode for use in a alkaline electrochemical cell, where the anode contains a metal anode active material, an anode electrolyte and an oxazoline surfactant.
  • the anode of the invention can include additional components known in the manufacture of alkaline electrochemical cells and anodes for same.
  • the invention relates to an alkaline electrochemical cell containing an anode of the invention.
  • the present invention relates to methods for making an anode of the invention, or for making a cell containing the anode, as are detailed below.
  • the anode, and an electrochemical cell containing the anode contain an oxazoline surfactant that can coat at least a portion of the particles of the anode active material.
  • It is an advantage of the present invention can maintain known benefits of anode surfactants, and can provide additional benefits that can include improved discharge efficiency at low and high rates, high operating voltage, lack of initial potential dip, and reduced sensitivity to open circuit rest.
  • FIG. 1 compares the discharge profiles of cells of the invention containing an oxazoline surfactant and cells containing an organosiliconate surfactant. Discharge was at 374 Ohm for 16 hours/day at 70° F., 50 % relative humidity, after one month storage at 70° F.
  • FIG. 2 compares the discharge profiles of cells of the invention containing an oxazoline surfactant and cells containing an organosiliconate surfactant. Discharge was at 620 Ohm for 16 hours/day at 70° F. 50 % relative humidity, after 20 days storage at 140° F.
  • the present invention relates to using an oxazoline-type surfactant, which can be a fatty oxazoline surfactant, as an additive for an alkaline electrochemical cell anode.
  • Cells comprising the anode can exhibit improved electrical discharge performance, including higher operating voltage, good high rate pulse capability, no initial potential dip and reduced sensitivity to open circuit rest in comparison to cells that use other surfactants.
  • Oxazoline-type surfactants can be added to anode materials of any alkaline metal-anode electrochemical cells to improve discharge performance and to improve discharge capacity, service-life, and shelf life. While the invention was exemplified with metal-air anodes and cells, more particularly in zinc-air cells, the invention can be employed in metal-containing anodes generally, more particularly in zinc anodes, and in cells containing same. Suitable chemistries include, but are not limited to, zinc-air, zinc-manganese dioxide, zinc/AgO and zinc/Ag 2 O systems, without regard to size or configuration. Preferable cells are of standard configurations, such as button cells, cylindrical cells and prismatic cells, which are available in a variety of standard sizes.
  • oxazoline type-surfactants can be substituted for the surfactants described in incorporated U.S. Pat. Nos. 4,857,424, 5,721,065 and 6,210,827.
  • the anode materials to which an oxazoline surfactant is added contain a metal powder, a gelling agent, and an electrolyte.
  • the anode materials can also include other components including but not limited to mercury, indium, gallium, aluminum, lead, bismuth and calcium compounds, and combinations thereof, as disclosed, for example, in the '065 patent and in U.S. Pat. No. 5,721,072, also incorporated herein by reference as if set forth in its entirety.
  • the present invention relates to an anode mix that includes a metal powder suitable for an anode of an alkaline electrochemical cell, an electrolyte compatible with the anode metal, an oxazoline surfactant and a gelling agent.
  • the present invention relates to an anode that includes the composition described above in a container for receiving the composition of matter.
  • the present invention relates to an alkaline electrochemical cell that contains the anode. The cell has a discharge voltage of at least 0.7 volts, preferably 1.0 volts, more preferably 1.1 volts and still more preferably 1.2 volts, during its service life.
  • the metal powder is preferably about 55% to about 73% by weight of the anode, the electrolyte is about 27% to about 45% (by weight) in an aqueous solution, and the oxazoline surfactant is about 0.001% to about 5% (by weight), based on the weight of the particles of metal powder.
  • the anode material generally also contains about 0.1% to about 0.5% of gelling agent, by weight based on the weight of active material, and between about 1% to about 4%, preferably about 2% of zinc oxide, by weight based on the weight of the electrolyte.
  • the metal powder is a particulate zinc alloy powder and the electrolyte is potassium hydroxide.
  • the present invention is a method of making an anode mix for use in the anode and in the cells of the invention, the method involving the steps of mixing a metal powder, a gelling agent, an oxazoline surfactant, and an electrolyte in the above-mentioned proportions.
  • the order in which the components are combined is not critical, except insofar as when mixing the oxazoline surfactant with a liquid (namely, the electrolyte or the gelled electrolyte), the surfactant is preferably a state (e.g., melted).
  • the surfactant is mixed first with the metal powder or other dry component, it can be a solid.
  • the gelling agent and the alkaline electrolyte are combined first to form a gelled electrolyte. Then, the oxazoline surfactant is added to the gelled electrolyte with agitation. Finally, the metal powder is combined with the surfactant-containing alkaline electrolyte to form the gelled zinc anode material which can be incorporated into the receiving container.
  • the present invention is a method of making an alkaline electrochemical cell involving the step of incorporating the aforementioned inventive anode into an electrochemical cell, the process for making the cell being, apart from the composition of the anode, conventional as is shown, for example in U.S. Pat. No. 4,617,242, incorporated herein by reference as if set forth in its entirety.
  • a suitable oxazoline surfactant can be solubilized in an anode-compatible electrolyte and is a liquid or can be liquefied under the anode processing conditions.
  • U.S. Pat. No. 3,389,145 incorporated by reference herein as if set forth in its entirety, discloses structures of one suitable set of oxazolines and processes for making same.
  • Also suitable for use in the anode of the invention are substituted oxazoline surfactants having the structures shown in U.S. Pat. No. 3,336,145, in U.S. Pat. No. 4,536,300, in U.S. Pat. No. 5,758,374 and in U.S. Pat. No.
  • Zinc air cells according to the invention were built with an anode as described in incorporated U.S. Pat. No. 4,617,242. except that the oxazoline surfactant was substituted at 0.3%, relative to the alkaline electrolyte in test cells in place of the organosiliconate surfactant of the prior anode composition.
  • the structure of the test and control cells was as described in incorporated U.S. Pat. No. 5,721,065.
  • FIG. 1 illustrates the discharge curve at 374 Ohm after 1 month storage of cells at 70° F.
  • FIG. 2 shows the discharge curve at 620 Ohm after 20 days storage at 140° F.
  • FIGS. 1 and 2 cells containing oxazoline-type surfactant-based exhibited operating voltage at least 5-10 mV higher than prior art cells during most of their usable lives.
  • the test cells did not exhibit an initial potential dip and were less sensitive to open circuit rest than otherwise comparable cells containing the organosiliconate type-surfactant.
  • Table 1 shows discharge capacity values at 374 Ohm of test cells containing Alkaterge T-IV surfactant. The capacity of these cells was comparable to that of organosiliconate type surfactant-based cells before and after storage for one month at 70° F., 50% relative humidity, although discharge capacity before storage was comparatively lower in cells that contained Alkaterge T-IV.

Abstract

According to the present invention an alkaline electrochemical cell can contain an anode having an anode active material, an alkaline electrolyte, a gelling agent and an oxazoline surfactant additive. The invention relates to an anode mix, to an anode containing the mix, and to an electrochemical cell containing the anode and to methods for making the anode mix, the anode and the cell. Performance improvements can be realized when the oxazoline surfactant is provided in the anode, which can include increased operating voltage, good high rate pulse capability, elimination of initial potential dip, good shelf life and reduced sensitivity to open circuit rest.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • Not applicable. [0001]
  • STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT
  • Not applicable. [0002]
  • BACKGROUND OF THE INVENTION
  • The demand for very small electrochemical cells has increased with increased use of small, electrically-powered devices, and alkaline and alkaline metal-air electrochemical cells are an increasingly popular choice for powering such devices as hearing appliances and computers. Metal air cells contain an anode and an oxygen cathode, with the oxygen usually obtained from ambient air. The oxygen cathode catalytically promotes the reaction of oxygen with an aqueous neutral or alkaline electrolyte and is not consumed or changed during discharge. As the cathode is extremely compact yet has essentially unlimited capacity, very high energy densities are achieved, resulting from the increased available volume for the anode active material. Consequently, a metal-air cell can provide more watt-hours of electromotive force than a so-called “two-electrode cell” of similar cell size, mass and anode composition that contains both anode- and cathode-active materials inside the cell structure. Metal-air cells have an advantageous watt-hour capacity/mass ratio without regard to size or configuration, which can be, e.g., button cells as in, for example, U.S. Pat. No. 5,721,065 (“the '065 patent”), or cylindrical cells as in, for example, U.S. Pat. No. 6,210,827 (the '827 patent”), each incorporated by reference in its entirety as if set forth herein. [0003]
  • A typical metal air cell such as a zinc air cell contains an anode that includes a zinc alloy powder, a carbon-based air cathode and an alkaline electrolyte with a gelling agent to prevent the electrolyte from creeping through the cell seals. For efficient operation, the anode of a zinc air cell should participate only during current-generating reaction periods. In reality, though, corrosive shelf-discharge side reactions in the alkaline electrolyte can reduce both service and shelf life of alkaline electrochemical systems that use zinc as the anode active material. Much effort has been directed to improving electrochemical reaction efficiency and cell output. Previously, mercury was added to cell anodes to improve corrosion resistance. In recent years, mercury has been replaced by substances that conform to environmental requirements. Small amounts of metals such as lead, indium, and bismuth, and combinations thereof, can effectively improve corrosion behavior of anodic zinc. Certain organic surfactants can provide effective corrosion-inhibiting effect at the metal surface while making the anode sufficiently available for electrochemical oxidation that the cell output can be maintained under heavy cell loading. Surfactants can, like mercury, improve discharge capacity, service life and shelf life, without substantial adverse environmental impact. U.S. Pat. No. 4,857,424 (“the '424 patent”) incorporated by reference herein as if set forth in its entirety, discloses reduced-mercury or mercury-free zinc-manganese dioxide cells containing an organosiliconate type surfactant. Also, the '065 patent discloses a button cell having an anode mix containing zinc metal powder, indium or other compounds, optionally a low level of mercury, a gelling agent and preferably a hydroxyethylcellulose surfactant. The anode disclosed therein sustains longer periods of power production at a relative steady voltage of at least 1.1 volts while protecting the anode metal from corrosion in the alkaline environment. [0004]
  • Similarly, the '827 patent discloses a cylindrical cell having an anode mix containing electrolyte, a gelling agent, particulate zinc, zinc oxide, additives and an organic surfactant comprising hydroxyethylcellulose. [0005]
  • Japanese Patent No. JP10083812 to Toshiba Battery Co. Ltd. discloses providing a high performance zinc alkaline battery containing 0.5-100 ppm of a fluorine-containing surfactant in a non-amalgamated-zinc-alloy-based gelled anode having a viscosity of 100,000 to 300,000 cPs at 25° C. [0006]
  • U.S. Pat. No. 5,382,482 concerns suppressing dendrites and shape change in an alkaline cell by disposing a cross-linked polymer film layer in close proximity to the anode active material, where the polymer film layer can contain, among other polymers, polyoxazoline. The patent does not describe including an oxazoline surfactant in the anode mix of the cell. [0007]
  • Further improvements in performance, such as increased operating voltage, improved discharge profile and reduced sensitivity to open circuit rest in alkaline electrochemical cells, preferably without sacrificing known benefits, are welcome and desired. [0008]
  • BRIEF SUMMARY OF THE INVENTION
  • The present invention discloses that an alkaline electrochemical cell having superior discharge performance and corrosion resistance includes an oxazoline surfactant additive in the cell anode. In one aspect, the present invention relates to an anode for use in a alkaline electrochemical cell, where the anode contains a metal anode active material, an anode electrolyte and an oxazoline surfactant. Optionally, the anode of the invention can include additional components known in the manufacture of alkaline electrochemical cells and anodes for same. In a related aspect, the invention relates to an alkaline electrochemical cell containing an anode of the invention. In another aspect, the present invention relates to methods for making an anode of the invention, or for making a cell containing the anode, as are detailed below. [0009]
  • It is an object of the invention to improve discharge performance and corrosion resistance without sacrificing the known benefits of adding surfactants to alkaline cell anodes. [0010]
  • It is a feature of the invention that the anode, and an electrochemical cell containing the anode, contain an oxazoline surfactant that can coat at least a portion of the particles of the anode active material. [0011]
  • It is an advantage of the present invention can maintain known benefits of anode surfactants, and can provide additional benefits that can include improved discharge efficiency at low and high rates, high operating voltage, lack of initial potential dip, and reduced sensitivity to open circuit rest. [0012]
  • Other objects, features and advantages of the present invention will become apparent in view of the following detailed description of the invention and the drawings.[0013]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 compares the discharge profiles of cells of the invention containing an oxazoline surfactant and cells containing an organosiliconate surfactant. Discharge was at 374 Ohm for 16 hours/day at 70° F., 50 % relative humidity, after one month storage at 70° F. [0014]
  • FIG. 2 compares the discharge profiles of cells of the invention containing an oxazoline surfactant and cells containing an organosiliconate surfactant. Discharge was at 620 Ohm for 16 hours/day at 70° F. 50 % relative humidity, after 20 days storage at 140° F.[0015]
  • DETAILED DESCRIPTION OF THE INVENTION
  • The present invention relates to using an oxazoline-type surfactant, which can be a fatty oxazoline surfactant, as an additive for an alkaline electrochemical cell anode. Cells comprising the anode can exhibit improved electrical discharge performance, including higher operating voltage, good high rate pulse capability, no initial potential dip and reduced sensitivity to open circuit rest in comparison to cells that use other surfactants. [0016]
  • Oxazoline-type surfactants can be added to anode materials of any alkaline metal-anode electrochemical cells to improve discharge performance and to improve discharge capacity, service-life, and shelf life. While the invention was exemplified with metal-air anodes and cells, more particularly in zinc-air cells, the invention can be employed in metal-containing anodes generally, more particularly in zinc anodes, and in cells containing same. Suitable chemistries include, but are not limited to, zinc-air, zinc-manganese dioxide, zinc/AgO and zinc/Ag[0017] 2O systems, without regard to size or configuration. Preferable cells are of standard configurations, such as button cells, cylindrical cells and prismatic cells, which are available in a variety of standard sizes. For example, oxazoline type-surfactants can be substituted for the surfactants described in incorporated U.S. Pat. Nos. 4,857,424, 5,721,065 and 6,210,827. The anode materials to which an oxazoline surfactant is added contain a metal powder, a gelling agent, and an electrolyte. The anode materials can also include other components including but not limited to mercury, indium, gallium, aluminum, lead, bismuth and calcium compounds, and combinations thereof, as disclosed, for example, in the '065 patent and in U.S. Pat. No. 5,721,072, also incorporated herein by reference as if set forth in its entirety.
  • In one aspect, the present invention relates to an anode mix that includes a metal powder suitable for an anode of an alkaline electrochemical cell, an electrolyte compatible with the anode metal, an oxazoline surfactant and a gelling agent. In another aspect, the present invention relates to an anode that includes the composition described above in a container for receiving the composition of matter. In still another aspect, the present invention relates to an alkaline electrochemical cell that contains the anode. The cell has a discharge voltage of at least 0.7 volts, preferably 1.0 volts, more preferably 1.1 volts and still more preferably 1.2 volts, during its service life. [0018]
  • In preferred embodiments, the metal powder is preferably about 55% to about 73% by weight of the anode, the electrolyte is about 27% to about 45% (by weight) in an aqueous solution, and the oxazoline surfactant is about 0.001% to about 5% (by weight), based on the weight of the particles of metal powder. The anode material generally also contains about 0.1% to about 0.5% of gelling agent, by weight based on the weight of active material, and between about 1% to about 4%, preferably about 2% of zinc oxide, by weight based on the weight of the electrolyte. In more preferred embodiments, the metal powder is a particulate zinc alloy powder and the electrolyte is potassium hydroxide. [0019]
  • In a related aspect, the present invention is a method of making an anode mix for use in the anode and in the cells of the invention, the method involving the steps of mixing a metal powder, a gelling agent, an oxazoline surfactant, and an electrolyte in the above-mentioned proportions. The order in which the components are combined is not critical, except insofar as when mixing the oxazoline surfactant with a liquid (namely, the electrolyte or the gelled electrolyte), the surfactant is preferably a state (e.g., melted). Alternatively, if the surfactant is mixed first with the metal powder or other dry component, it can be a solid. In one embodiment of the method, the gelling agent and the alkaline electrolyte are combined first to form a gelled electrolyte. Then, the oxazoline surfactant is added to the gelled electrolyte with agitation. Finally, the metal powder is combined with the surfactant-containing alkaline electrolyte to form the gelled zinc anode material which can be incorporated into the receiving container. [0020]
  • In another related aspect, the present invention is a method of making an alkaline electrochemical cell involving the step of incorporating the aforementioned inventive anode into an electrochemical cell, the process for making the cell being, apart from the composition of the anode, conventional as is shown, for example in U.S. Pat. No. 4,617,242, incorporated herein by reference as if set forth in its entirety. [0021]
  • A suitable oxazoline surfactant can be solubilized in an anode-compatible electrolyte and is a liquid or can be liquefied under the anode processing conditions. U.S. Pat. No. 3,389,145, incorporated by reference herein as if set forth in its entirety, discloses structures of one suitable set of oxazolines and processes for making same. Also suitable for use in the anode of the invention are substituted oxazoline surfactants having the structures shown in U.S. Pat. No. 3,336,145, in U.S. Pat. No. 4,536,300, in U.S. Pat. No. 5,758,374 and in U.S. Pat. No. 5,407,500, each incorporated by reference herein as if set forth in its entirety, and mixtures of any of the foregoing. A most preferred oxazoline surfactant, ethanol, 2,2′-[(2-heptadecyl-4(5H)-oxazolydine) bis (methyleneoxy-2,1-ethanedyloxy]bis, has a structure shown as Formula (I-2) in incorporated U.S. Pat. No. 5,407,500. This compound is commercially available from Angus Chemical (Northbrook, Ill.) as Alkaterge T-IV. [0022]
  • EXAMPLE
  • Zinc air cells according to the invention were built with an anode as described in incorporated U.S. Pat. No. 4,617,242. except that the oxazoline surfactant was substituted at 0.3%, relative to the alkaline electrolyte in test cells in place of the organosiliconate surfactant of the prior anode composition. The structure of the test and control cells was as described in incorporated U.S. Pat. No. 5,721,065. [0023]
  • The discharge characteristics of 13 size zinc air cells of the present invention containing Alkaterge T-IV were compared against otherwise identical commercial cells having an organosiliconate surfactant in the anode. FIG. 1 illustrates the discharge curve at 374 Ohm after 1 month storage of cells at 70° F.; FIG. 2 shows the discharge curve at 620 Ohm after 20 days storage at 140° F. As shown in FIGS. 1 and 2, cells containing oxazoline-type surfactant-based exhibited operating voltage at least 5-10 mV higher than prior art cells during most of their usable lives. In addition, the test cells did not exhibit an initial potential dip and were less sensitive to open circuit rest than otherwise comparable cells containing the organosiliconate type-surfactant. [0024]
  • Further, Table 1 shows discharge capacity values at 374 Ohm of test cells containing Alkaterge T-IV surfactant. The capacity of these cells was comparable to that of organosiliconate type surfactant-based cells before and after storage for one month at 70° F., 50% relative humidity, although discharge capacity before storage was comparatively lower in cells that contained Alkaterge T-IV. [0025]
    TABLE 1
    Discharge Capacity (mAh) at 1.1 Volt
    Control Alkaterge T-IV Alkaterge T Alkaterge E
    No Delay 251 244 247 N/A
    One month 252 252 198 N/A
  • Additionally, cells containing Alkaterge T-IV and control cells were also stored for twenty days at 140° F., 50% relative humidity and were tested at 620 Ohm for 16 hours/day at 70° F., 50% relative humidity. Results of the two cell types were comparable (258 mAh v. 254 mAh, respectively). [0026]
  • Taken together these results demonstrate that oxazoline-type surfactants can effectively maintain cell capacity. Also, oxazoline-type surfactant based cells exhibited good high rate pulse capability as compared to the control cells. [0027]

Claims (15)

I claim:
1. An anode mix comprising an alkaline electrolyte, an anode active material, a gelling agent and an oxazoline surfactant.
2. The anode mix of claim 1 wherein the oxazoline surfactant comprises a fatty side chain.
3. The anode mix of claim 2 wherein the oxazoline surfactant is ethanol, 2,2′-[(2-heptadecyl-4(5H)-oxazolydine) bis (methyleneoxy-2,1 -ethanedyloxy]bis.
4. The anode mix of claim 2 wherein the oxazoline surfactant comprising the fatty side chain is Alkaterge T-IV.
5. The anode mix of claim 1, wherein the alkaline electrolyte is potassium hydroxide.
6. The anode mix of claim 1, wherein the anode active material is particulate zinc powder.
7. The anode mix of claim 1, wherein the surfactant coats at least a portion of the anode active material.
8. An anode for use in an electrochemical cell, the anode comprising the anode mix of any of claims 1-7.
9. An alkaline electrochemical cell comprising a cathode, an anode, and an alkaline electrolyte in electrical contact with the anode and the cathode, the anode comprising an anode active material, a gelling agent and an oxazoline surfactant.
10. The alkaline electrochemical cell of claim 9 wherein the oxazoline surfactant comprises a fatty side chain.
11. The alkaline electrochemical cell of claim 10 wherein the oxazoline surfactant is ethanol, 2,2′-[(2-heptadecyl-4(5H)-oxazolydine) bis (methyleneoxy-2,1-ethanedyloxy]bis.
12. The alkaline electrochemical cell of claim 10 wherein the oxazoline surfactant comprising the fatty side chain is Alkaterge T-IV.
13. The alkaline electrochemical cell of claim 9 wherein the alkaline electrolyte is potassium hydroxide.
14. The alkaline electrochemical cell of claim 9 wherein the anode active material is particulate zinc powder.
15. The alkaline electrochemical cell of claim 9 wherein the surfactant coats at least a portion of the anode active material.
US10/020,685 2001-12-14 2001-12-14 Oxazoline surfactant anode additive for alkaline electrochemical cells Abandoned US20030113623A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
US10/020,685 US20030113623A1 (en) 2001-12-14 2001-12-14 Oxazoline surfactant anode additive for alkaline electrochemical cells
AT02797314T ATE556445T1 (en) 2001-12-14 2002-12-13 OXAZOLINE SURFACTANT ADDITIVES FOR ALKALINE ELECTROCHEMICAL CELLS
EP02797314A EP1506584B1 (en) 2001-12-14 2002-12-13 Oxazoline surfactant anode additive for alkaline electrochemical cells
AU2002361674A AU2002361674A1 (en) 2001-12-14 2002-12-13 Oxazoline surfactant anode additive for alkaline electrochemical cells
PCT/US2002/039990 WO2003052843A2 (en) 2001-12-14 2002-12-13 Oxazoline surfactant anode additive for alkaline electrochemical cells
US10/944,036 US6927000B2 (en) 2001-12-14 2004-09-17 Oxazoline surfactant anode additive for alkaline electrochemical cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/020,685 US20030113623A1 (en) 2001-12-14 2001-12-14 Oxazoline surfactant anode additive for alkaline electrochemical cells

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US10/944,036 Continuation US6927000B2 (en) 2001-12-14 2004-09-17 Oxazoline surfactant anode additive for alkaline electrochemical cells

Publications (1)

Publication Number Publication Date
US20030113623A1 true US20030113623A1 (en) 2003-06-19

Family

ID=21799985

Family Applications (2)

Application Number Title Priority Date Filing Date
US10/020,685 Abandoned US20030113623A1 (en) 2001-12-14 2001-12-14 Oxazoline surfactant anode additive for alkaline electrochemical cells
US10/944,036 Expired - Lifetime US6927000B2 (en) 2001-12-14 2004-09-17 Oxazoline surfactant anode additive for alkaline electrochemical cells

Family Applications After (1)

Application Number Title Priority Date Filing Date
US10/944,036 Expired - Lifetime US6927000B2 (en) 2001-12-14 2004-09-17 Oxazoline surfactant anode additive for alkaline electrochemical cells

Country Status (5)

Country Link
US (2) US20030113623A1 (en)
EP (1) EP1506584B1 (en)
AT (1) ATE556445T1 (en)
AU (1) AU2002361674A1 (en)
WO (1) WO2003052843A2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070122709A1 (en) * 2005-11-30 2007-05-31 Rovcal, Inc. Ionically conductive clay additive for use in electrochemical cells
WO2015057808A1 (en) * 2013-10-15 2015-04-23 Eaglepicher Technologies, Llc High energy density non-aqueous electro-chemical cell
US9403999B2 (en) * 2014-04-01 2016-08-02 Angus Chemical Company Oxazoline compounds as open-time extenders for latex paints

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6872489B2 (en) * 2002-02-27 2005-03-29 Rovcal, Inc. Alkaline cell with gassing inhibitors
US7226696B2 (en) * 2002-02-27 2007-06-05 Rayovac Corporation Alkaline cell with performance enhancing additives
US20070048576A1 (en) * 2005-08-30 2007-03-01 Rovcal, Inc. Electrochemical cells containing spun mercury-amalgamated zinc particles having improved physical characteristics
US20070048575A1 (en) * 2005-08-30 2007-03-01 Rovcal, Inc. Electrochemical cells containing spun mercury-amalgamated zinc particles having improved physical characteristics
US9136540B2 (en) 2005-11-14 2015-09-15 Spectrum Brands, Inc. Metal air cathode manganese oxide contained in octahedral molecular sieve
US20070122699A1 (en) * 2005-11-30 2007-05-31 Rovcal, Inc. Electrochemical cells having improved gelling agents
US20080193851A1 (en) * 2007-02-09 2008-08-14 Rovcal, Inc. Alkaline electrochemical cell having improved gelled anode
EP2973627B1 (en) 2013-03-13 2021-09-01 Form Energy, Inc. Hetero-ionic aromatic additives for electrochemical cells comprising a metal fuel
US10381643B2 (en) 2014-10-08 2019-08-13 Energizer Brands, Llc Fluorosurfactant as a zinc corrosion inhibitor
US10205206B2 (en) 2014-10-08 2019-02-12 Energizer Brands, Llc Zinc-air electrochemical cell
US10319991B2 (en) 2014-10-23 2019-06-11 Energizer Brands, Llc Zinc anode composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5698339A (en) * 1994-10-21 1997-12-16 Canon Kabushiki Kaisha Anode with an anode active material-retaining body having a number of pores distributed therein, a rechargeable battery, provided with said anode, and the process for the production of said anode

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3336145A (en) 1964-03-20 1967-08-15 Commercial Solvents Corp Nitrocellulose coating composition plasticized with oxazolines
US3389145A (en) 1965-10-24 1968-06-18 Katz Jacob Fatty oxazoline surfactants and a process for their preparation
US3965082A (en) 1973-10-15 1976-06-22 Commercial Solvents Corporation Compositions of polystyrene reacted with hexamethoxymethylmelamine
US4536300A (en) 1981-07-20 1985-08-20 Angus Chemical Company Micellar solution for recovering crude oil
US4489144A (en) * 1983-03-28 1984-12-18 Union Carbide Corporation Isoxazole derivative additive in organic electrolytes of nonaqueous cells employing solid cathodes
US4617242A (en) * 1983-10-19 1986-10-14 Rayovac Corporation Organic siliconate additive for alkaline zinc electrochemical cells
US4828633A (en) * 1987-12-23 1989-05-09 The Lubrizol Corporation Salt compositions for explosives
US4758374A (en) * 1987-03-17 1988-07-19 Conoco Inc. Soluble oil concentrate and emulsifier system used therein
US4857424A (en) * 1988-10-11 1989-08-15 Rayovac Corporation Zinc alkaline electrochemical cells with reduced mercury anodes
JPH0371559A (en) 1989-08-10 1991-03-27 Sanyo Electric Co Ltd Zinc alkaline battery
US5382482A (en) 1992-08-07 1995-01-17 Nippon Oil Company, Limited Zinc electrode for alkaline storage battery
US5439978A (en) 1993-08-09 1995-08-08 Sri International Oxazine -and oxazoline-based copolymers useful as antielectrostatic agents and polymeric compositions prepared therewith
DE69602122T2 (en) 1995-03-07 1999-08-19 Matsushita Electric Ind Co Ltd Flat cell
US5721065A (en) 1995-05-05 1998-02-24 Rayovac Corporation Low mercury, high discharge rate electrochemical cell
JP3370486B2 (en) 1995-07-21 2003-01-27 松下電器産業株式会社 Alkaline battery
JP4355800B2 (en) 1996-09-11 2009-11-04 東芝電池株式会社 Zinc alkaline battery
JP3439083B2 (en) 1997-08-04 2003-08-25 三洋電機株式会社 Non-aqueous electrolyte battery
US6255021B1 (en) * 1997-08-04 2001-07-03 Sanyo Electric Co., Ltd. Lithium battery including storage stabilized dioxolane-containing electrolyte
JP3439084B2 (en) 1997-08-05 2003-08-25 三洋電機株式会社 Non-aqueous electrolyte battery
JPH11181476A (en) 1997-12-25 1999-07-06 Kao Corp Surfactant mixture
US6197445B1 (en) 1998-03-06 2001-03-06 Rayovac Corporation Air depolarized electrochemical cells
EP1393393B1 (en) * 2001-05-24 2011-05-11 Rayovac Corporation Ionically conductive additive for zinc-based anode in alkaline electrochemical cells

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5698339A (en) * 1994-10-21 1997-12-16 Canon Kabushiki Kaisha Anode with an anode active material-retaining body having a number of pores distributed therein, a rechargeable battery, provided with said anode, and the process for the production of said anode

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070122709A1 (en) * 2005-11-30 2007-05-31 Rovcal, Inc. Ionically conductive clay additive for use in electrochemical cells
US7563537B2 (en) 2005-11-30 2009-07-21 Rovcal, Inc. Ionically conductive clay additive for use in electrochemical cells
WO2015057808A1 (en) * 2013-10-15 2015-04-23 Eaglepicher Technologies, Llc High energy density non-aqueous electro-chemical cell
US9991493B2 (en) * 2013-10-15 2018-06-05 Eaglepicher Technologies, Llc High energy density non-aqueous electrochemical cell with extended operating temperature window
US9403999B2 (en) * 2014-04-01 2016-08-02 Angus Chemical Company Oxazoline compounds as open-time extenders for latex paints

Also Published As

Publication number Publication date
WO2003052843A3 (en) 2004-11-18
AU2002361674A1 (en) 2003-06-30
ATE556445T1 (en) 2012-05-15
US6927000B2 (en) 2005-08-09
EP1506584A2 (en) 2005-02-16
EP1506584B1 (en) 2012-05-02
WO2003052843A2 (en) 2003-06-26
US20050031956A1 (en) 2005-02-10

Similar Documents

Publication Publication Date Title
EP1393393B1 (en) Ionically conductive additive for zinc-based anode in alkaline electrochemical cells
US7563537B2 (en) Ionically conductive clay additive for use in electrochemical cells
Shen et al. The mechanism of capacity fade of rechargeable alkaline manganese dioxide zinc cells
US6927000B2 (en) Oxazoline surfactant anode additive for alkaline electrochemical cells
JP4319253B2 (en) Electrochemical battery zinc anode
CA2189341A1 (en) Sealed rechargeable cells containing mercury-free zinc anodes, and a method of manufacture
JPH08510355A (en) Additive for primary electrochemical cells with manganese dioxide cathode
US4379815A (en) Cell having mixed solid cathode materials for controlling cell expansion on discharge
JP2004513501A (en) Positive and negative interaction electrode formulation for zinc containing cells with alkaline electrolyte
US7160647B2 (en) Battery cathode
JP2003502808A (en) Alkaline battery with improved anode
JP5172181B2 (en) Zinc alkaline battery
WO2003071653A2 (en) Cylindrical alkaline cells with increased discharge performance
EP0077614A2 (en) Alkaline electrochemical cells
WO2004012886B1 (en) Zinc powders for use in electrochemical cells
US20070122699A1 (en) Electrochemical cells having improved gelling agents
US20090202910A1 (en) Alkaline Batteries
US20070048576A1 (en) Electrochemical cells containing spun mercury-amalgamated zinc particles having improved physical characteristics
EP1293002B1 (en) Electrochemical cells with an anode containing sulfur
US20070048575A1 (en) Electrochemical cells containing spun mercury-amalgamated zinc particles having improved physical characteristics
JP3315530B2 (en) Alkaline battery
JP3094589B2 (en) Manganese dry battery manufacturing method
JP2001297776A (en) Alkali cell
JPH05151957A (en) Alkaline battery
AU2002303771A1 (en) Ionically conductive additive for zinc-based anode in alkaline electrochemical cells

Legal Events

Date Code Title Description
AS Assignment

Owner name: RAYOVAC CORPORATION, WISCONSIN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:NDZEBET, ERNEST;REEL/FRAME:012599/0029

Effective date: 20020128

AS Assignment

Owner name: ROVCAL, INC., CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:RAYOVAC CORPORATION;REEL/FRAME:015370/0034

Effective date: 20031112

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION