US20060035145A1 - Lead-zinc battery - Google Patents
Lead-zinc battery Download PDFInfo
- Publication number
- US20060035145A1 US20060035145A1 US11/249,223 US24922305A US2006035145A1 US 20060035145 A1 US20060035145 A1 US 20060035145A1 US 24922305 A US24922305 A US 24922305A US 2006035145 A1 US2006035145 A1 US 2006035145A1
- Authority
- US
- United States
- Prior art keywords
- lead
- zinc
- electrolyte
- cell
- battery
- 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
Links
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/56—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of lead
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/08—Selection of materials as electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/20—Semi-lead accumulators, i.e. accumulators in which only one electrode contains lead
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/24—Alkaline accumulators
- H01M10/26—Selection of materials as electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/244—Zinc electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0002—Aqueous electrolytes
- H01M2300/0014—Alkaline electrolytes
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/60—Other road transportation technologies with climate change mitigation effect
- Y02T10/70—Energy storage systems for electromobility, e.g. batteries
Definitions
- the present invention relates to a novel type of storage battery which is distinguished by its unique electrochemistry.
- the positive electrode comprises lead dioxide and the negative electrode zinc.
- the electrolyte consists of an alkaline aqueous solution of an alkali metal hydroxide or tetramethyl ammonium hydroxide to which various buffers, including carbonates, borates, silicates, and phosphates, may be added. Upon discharge the lead dioxide is reduced to lead oxide and the zinc is oxidized to zinc oxide.
- the most common storage battery found in almost every vehicle, is the lead-acid battery.
- This battery comprises a lead dioxide positive electrode, a lead metal negative electrode, and sulfuric acid for the electrolyte. Its chief advantage is low cost. Nevertheless, it has a limited energy density and the electrolyte is extremely corrosive. Furthermore, sufficient acid is required to react with the electrodes during discharge. Maintenance-free types avoid the loss of evolved gases, as disclosed in U.S. Pat. No. 3,862,861, but their cycle-life is still restricted.
- a storage battery is fabricated from a positive electrode of lead and a negative electrode of zinc. During charging some lead is converted to lead dioxide. Upon discharge lead dioxide is reduced to lead oxide and zinc is oxidized to zinc oxide. These reactions are reversible such that the battery fulfills both functions of a secondary battery: supplying electricity on demand and storing or accumulating surplus electricity.
- the electrolyte of a cell is alkaline.
- Aqueous solutions of bases provide the alkalinity.
- bases include ammonia and the hydroxides of the alkali metals, namely, lithium, sodium, potassium and cesium.
- tetramethyl ammonium hydroxide may be employed.
- additives have been found to be effective buffers in the electrolyte. These additives include carbonates, borates, silicates and phosphates. They may be introduced by the corresponding acids or their respective salts.
- the electrodes of a practical embodiment of the invention may be configured as sheets, fibers, or particles thereby to maximize electrode surface area. Interspersed particles of a carbonaceous material may be used to improve the electrical conductivity. A gelling agent may be added to immobilize the electrolyte. As required, a separator may be employed between the positive and negative electrodes to prevent a short circuit.
- a positive electrode comprises lead dioxide which is reduced to lead oxide during discharge.
- the negative electrode comprises zinc which is oxidized to zinc oxide when the cell is discharged.
- the electrolyte is alkaline such that the solution contains an excess of hydroxyl ions.
- Negative electrode Zn+2OH ⁇ ⁇ ZnO+H 2 O+2e ⁇ (2)
- zinc hydroxide may be an intermediate in the formation of zinc oxide.
- the reaction for the cell is: PbO 2 +Zn ⁇ PbO+ZnO (3)
- the overall reaction there is no change in the average composition of the electrolyte during discharge although there may be concentration gradients.
- a particularly difficult challenge in designing new batteries is identifying electrode materials that will undergo electrochemical reactions and still withstand corrosion by the electrolyte. Although theory is helpful in this respect, empirical data are required to prove the effectiveness of materials—both for the electrodes and the electrolyte.
- One measure of the relative performance of a cell is its open-circuit voltage.
- borates can be employed to similar advantage.
- Boric acid is a weak acid, much more mild than carbonic acid. Thus, its salts tend to hydrolyze in solution.
- the following equation shows the reaction of potassium meta borate in solution to form potassium hydroxide and potassium tetra borate. 2K 2 B 2 O 4 +H 2 O 2KOH+K 2 B 4 O 7 (5) Again the hydroxyl concentration can be controlled by adjusting the concentration of the potassium borate.
- Carbonates and borates are effective not only in controlling the alkalinity of the electrolyte, but they also form insoluble salts with lead and zinc. In this manner the corrosion of such electrodes can be minimized. Not only are carbonates and borates helpful in this regard, but other salts are likewise effective. Both silicates and phosphates form insoluble salts with lead and zinc.
- Alkalinity can be provided by compounds of the alkali metals including lithium, sodium, potassium, and cesium. Lithium has certain limitations inasmuch as its carbonate and phosphate are almost insoluble in water. Cesium provides a very strong base but the cost of this material limits its potential applications. While ammonium hydroxide is basic in solution, its volatility restricts its use. Finally, tetramethyl ammonium hydroxide is known to be strongly alkaline, approaching that of sodium hydroxide and potassium hydroxide.
- the present invention covers the use of aqueous solutions for the electrolyte. These solutions have the advantage of superior electrical conductivities. Although use of organic solvents including alcohols and glycols is feasible, their performance is inferior.
- a lead-zinc cell is not restricted.
- a simple cell was assembled from a glass jar and strips of metals separated, as need be, by a polypropylene sheet.
- a workable battery would necessarily be designed with the maximum surface areas for the electrodes and minimum volume of electrolyte.
- Such geometric designs as parallel plates, either flat or spirally wound, are appropriate.
- particles of lead and zinc either alone or interspersed with graphite may be employed. In this manner, the capacity of the cell can be increased and its internal resistance minimized.
- FIG. 1 illustrates its distinctive features.
- the cut-away perspective shows a lead-zinc battery comprising a single cell with its electrodes arranged as flat parallel plates.
- the lead positive electrodes 1 and the zinc negative electrodes 2 are kept apart by separators 3 .
- These parts are immersed in the alkaline electrolyte 4 , which is contained in casing 5 .
- This sectional view also shows the electrical leads attached to the electrodes.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Inorganic Chemistry (AREA)
- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
A rechargeable battery is provided such that the positive electrode comprises lead dioxide, the negative electrode zinc, and the electrolyte is alkaline. Upon discharge, the lead dioxide is reduced to lead oxide, the zinc is oxidized to zinc oxide, and the electrolyte remains unchanged. The reactions are reversed when the battery is charged.
Description
- This application is a continuation of U.S. application Ser. No. 10/756,015 filed under attorney docket no. STF-122-A on Jan. 13, 2004, currently pending.
- The present invention relates to a novel type of storage battery which is distinguished by its unique electrochemistry. The positive electrode comprises lead dioxide and the negative electrode zinc. The electrolyte consists of an alkaline aqueous solution of an alkali metal hydroxide or tetramethyl ammonium hydroxide to which various buffers, including carbonates, borates, silicates, and phosphates, may be added. Upon discharge the lead dioxide is reduced to lead oxide and the zinc is oxidized to zinc oxide.
- The most common storage battery, found in almost every vehicle, is the lead-acid battery. This battery comprises a lead dioxide positive electrode, a lead metal negative electrode, and sulfuric acid for the electrolyte. Its chief advantage is low cost. Nevertheless, it has a limited energy density and the electrolyte is extremely corrosive. Furthermore, sufficient acid is required to react with the electrodes during discharge. Maintenance-free types avoid the loss of evolved gases, as disclosed in U.S. Pat. No. 3,862,861, but their cycle-life is still restricted.
- The search for alternatives to the lead-acid battery has been ongoing. As far back as 1934, Drumm disclosed the nickel oxide-zinc battery and the silver oxide-zinc battery (U.S. Pat. No. 1,955,115). Both of these batteries employ zinc as the negative electrode and caustic potash as the electrolyte. Nickel oxide or silver oxide serves as the positive electrode. These batteries have improved energy densities and for many uses are a good compromise.
- The ideal storage battery would combine the best features of existing batteries with none of the drawbacks. The need for such a battery is apparent for backup systems and in mobile applications. Therefore, it is an object of the present invention to provide an improved storage battery, one that is both economical and highly efficient. These and other objects, features, and advantages of the invention will be recognized from the following description and accompanying figure.
- A storage battery is fabricated from a positive electrode of lead and a negative electrode of zinc. During charging some lead is converted to lead dioxide. Upon discharge lead dioxide is reduced to lead oxide and zinc is oxidized to zinc oxide. These reactions are reversible such that the battery fulfills both functions of a secondary battery: supplying electricity on demand and storing or accumulating surplus electricity.
- The electrolyte of a cell is alkaline. Aqueous solutions of bases provide the alkalinity. These bases include ammonia and the hydroxides of the alkali metals, namely, lithium, sodium, potassium and cesium. In addition, tetramethyl ammonium hydroxide may be employed.
- Certain additives have been found to be effective buffers in the electrolyte. These additives include carbonates, borates, silicates and phosphates. They may be introduced by the corresponding acids or their respective salts.
- The electrodes of a practical embodiment of the invention may be configured as sheets, fibers, or particles thereby to maximize electrode surface area. Interspersed particles of a carbonaceous material may be used to improve the electrical conductivity. A gelling agent may be added to immobilize the electrolyte. As required, a separator may be employed between the positive and negative electrodes to prevent a short circuit.
- The chemistry of the lead-zinc battery is important in order to gain an understanding of its operation. A positive electrode comprises lead dioxide which is reduced to lead oxide during discharge. The negative electrode comprises zinc which is oxidized to zinc oxide when the cell is discharged. The electrolyte is alkaline such that the solution contains an excess of hydroxyl ions. The electrode reactions during discharge can be represented by the following equations:
- Positive electrode:
PbO2+H2O+2e−→PbO+2OH− (1) - Negative electrode:
Zn+2OH−→ZnO+H2O+2e− (2)
In the above reaction, zinc hydroxide may be an intermediate in the formation of zinc oxide. When these equations are combined, the reaction for the cell is:
PbO2+Zn→PbO+ZnO (3)
In the overall reaction, there is no change in the average composition of the electrolyte during discharge although there may be concentration gradients. - During recharging of the cell, the reactions are reversed. Thus, lead oxide is oxidized to lead dioxide and zinc oxide is reduced to zinc metal. The emf necessary for charging is supplied by an external power source. The discharge-recharge cycle can be repeated endlessly, thus fulfilling the function of a storage battery.
- A particularly difficult challenge in designing new batteries is identifying electrode materials that will undergo electrochemical reactions and still withstand corrosion by the electrolyte. Although theory is helpful in this respect, empirical data are required to prove the effectiveness of materials—both for the electrodes and the electrolyte. One measure of the relative performance of a cell is its open-circuit voltage.
- The use of lead in an alkaline cell may seem questionable because lead in the +2 oxidation state commonly forms plumbous salts containing the positive divalent ion Pb++. However, by the action of hydroxides on plumbous compounds it is possible to form the negative ion HPbO2 − which is soluble in aqueous solutions. Accordingly Pb(OH)2 is regarded as an amphoteric hydroxide. In a similar manner, concentrated solutions of alkali hydroxides act upon the dioxide PbO2 to form plumbate ions, PbO4−4 and PbO3 −2, which are likewise soluble.
- In view of these considerations, one goal of the research on new cells was to control the concentration hydroxides in the electrolyte. This result was made possible by employing solutions of sodium carbonate which react as follows:
Na2CO3+H2ONaOH+NaHCO3 (4)
From this equation it is seen that such solutions are strongly alkaline. The carbonic acid set free on hydrolysis does not escape when the base is strong but forms the bicarbonate. However, hydrolysis can be reduced by increasing the concentration of the sodium carbonate, thus permitting a degree of control over the formation of hydroxide. - In place of carbonates, borates can be employed to similar advantage. Boric acid is a weak acid, much more mild than carbonic acid. Thus, its salts tend to hydrolyze in solution. The following equation shows the reaction of potassium meta borate in solution to form potassium hydroxide and potassium tetra borate.
2K2B2O4+H2O2KOH+K2B4O7 (5)
Again the hydroxyl concentration can be controlled by adjusting the concentration of the potassium borate. - Carbonates and borates are effective not only in controlling the alkalinity of the electrolyte, but they also form insoluble salts with lead and zinc. In this manner the corrosion of such electrodes can be minimized. Not only are carbonates and borates helpful in this regard, but other salts are likewise effective. Both silicates and phosphates form insoluble salts with lead and zinc.
- Alkalinity can be provided by compounds of the alkali metals including lithium, sodium, potassium, and cesium. Lithium has certain limitations inasmuch as its carbonate and phosphate are almost insoluble in water. Cesium provides a very strong base but the cost of this material limits its potential applications. While ammonium hydroxide is basic in solution, its volatility restricts its use. Finally, tetramethyl ammonium hydroxide is known to be strongly alkaline, approaching that of sodium hydroxide and potassium hydroxide.
- The present invention covers the use of aqueous solutions for the electrolyte. These solutions have the advantage of superior electrical conductivities. Although use of organic solvents including alcohols and glycols is feasible, their performance is inferior.
- The configuration of a lead-zinc cell is not restricted. For purposes of testing various combinations of electrodes and electrolytes, a simple cell was assembled from a glass jar and strips of metals separated, as need be, by a polypropylene sheet. A workable battery, however, would necessarily be designed with the maximum surface areas for the electrodes and minimum volume of electrolyte. Such geometric designs as parallel plates, either flat or spirally wound, are appropriate. Alternatively, particles of lead and zinc either alone or interspersed with graphite may be employed. In this manner, the capacity of the cell can be increased and its internal resistance minimized.
- To gain a greater appreciation of the present invention,
FIG. 1 illustrates its distinctive features. The cut-away perspective shows a lead-zinc battery comprising a single cell with its electrodes arranged as flat parallel plates. The leadpositive electrodes 1 and the zincnegative electrodes 2 are kept apart byseparators 3. These parts are immersed in thealkaline electrolyte 4, which is contained incasing 5. This sectional view also shows the electrical leads attached to the electrodes. An advantage of this design is that by placing the positive and negative electrodes in close proximity to each other the quantity of electrolyte is reduced. - Applications of a secondary battery as provided by the present invention are almost limitless. The largest application is in vehicles including automobiles powered by new hybrid motors. Other uses include portable electronic devices such as cell phones and laptop computers.
-
-
- 1. The electrolyte in this example contained sodium carbonate. The sodium carbonate solution was prepared by heating 96.8 g. of baking soda (sodium bicarbonate) to 500° F. and dissolving the product in 185 ml. of water. The positive electrode was formed from a 1½ in. wide strip of lead obtained from a plumbing supply business. The negative electrode was a 1½ in. wide strip of zinc which had been removed from a flashlight battery of the Leclanche type. The cell compromised a glass jar about 2¾ in. diameter by 2½ in. high. After charging the cell for 23 minutes at 2.50 v., an open circuit voltage of 2.32 v. was observed for the cell. The cell was repeatedly discharged and charged during the course of the run. At the end of the experiment, the electrodes were in perfect condition and the electrolyte was water-white.
- 2. In this run the electrolyte was a solution of potassium borate. The same electrodes and container were used as in example 1. To prepare the electrolyte 40.0 g. of potassium hydroxide and 44.5 g. of boric acid were dissolved in 175 ml. of water. After charging the cell for 39 minutes at 2.50 v., the open circuit voltage of the cell was 2.1 v. No corrosion was apparent on either electrode at the end of the run.
- 3. Tetramethyl ammonium borate was employed for the electrolyte. The same electrodes were used as in the prior runs, but a
smaller glass jar 2 in. diameter by 3¾ in. high was substituted. The electrolyte was prepared by dissolving 50.0 g. of tetramethyl ammonium hydroxide pentahydrate and 19.9 g. of boric acid in 100 ml. water. An open-circuit voltage of 2.18 v. was obtained after charging the cell at 2.50 v. for 32 minutes. Both electrodes were in excellent condition at the end of the run. - 4. In this case the electrolyte comprised sodium hydroxide, sodium carbonate, sodium silicate and sodium phosphate. The electrodes and cell were identical to the ones in the previous run. The electrolyte was prepared by adding 50.1 g. of a household dishwasher detergent to 160 ml. water. The detergent contained sodium carbonate, sodium silicate, enzymes, and 7.4% phosphorous in the form of phosphates. Activated carbon was added to the solution before filtering it through four coffee filter papers. 125 ml. of filtrate was obtained. Next 5.0 g. of sodium hydroxide was added to the filtrate to produce the electrolyte. After extensive charging at 2.5 v., an open-circuit voltage of 2.1 v. was realized. The cell capacity was equal to or better than the results for any of the other runs. The electrodes were in perfect condition at the end of the experiment.
Claims (4)
1. A storage battery comprising:
(a) a positive electrode of lead;
(b) a negative electrode of zinc; and
(c) an alkaline electrolyte.
2. A storage battery of claim 1 in which the alkaline electrolyte is an aqueous solution of a hydroxide of an alkali metal selected from the group lithium, sodium, potassium, and cesium.
3. A storage battery of claim 1 in which the alkaline electrolyte is an aqueous solution of tetramethyl ammonium hydroxide.
4. A storage battery of claim 1 in which the alkaline electrolyte contains a buffering agent selected from the group carbonates, borates, silicates, and phosphates.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/249,223 US20060035145A1 (en) | 2004-01-13 | 2005-10-13 | Lead-zinc battery |
US11/763,029 US7682737B2 (en) | 2004-01-13 | 2007-06-14 | Lead-zinc storage battery |
US12/608,201 US20100047697A1 (en) | 2004-01-13 | 2009-10-29 | Lead-zinc battery |
US13/649,601 US20130045415A1 (en) | 2004-01-13 | 2012-10-11 | Lead-zinc battery |
US13/901,157 US20130252083A1 (en) | 2004-01-13 | 2013-05-23 | Lead-zinc battery |
US14/267,202 US9147912B2 (en) | 2004-01-13 | 2014-05-01 | Method of producing an electrical potential |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/756,015 US20050153203A1 (en) | 2004-01-13 | 2004-01-13 | Lead-zinc battery |
US11/249,223 US20060035145A1 (en) | 2004-01-13 | 2005-10-13 | Lead-zinc battery |
Related Parent Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/756,015 Continuation-In-Part US20050153203A1 (en) | 2004-01-13 | 2004-01-13 | Lead-zinc battery |
US10/756,015 Continuation US20050153203A1 (en) | 2004-01-13 | 2004-01-13 | Lead-zinc battery |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/763,029 Continuation US7682737B2 (en) | 2004-01-13 | 2007-06-14 | Lead-zinc storage battery |
US12/608,201 Continuation-In-Part US20100047697A1 (en) | 2004-01-13 | 2009-10-29 | Lead-zinc battery |
Publications (1)
Publication Number | Publication Date |
---|---|
US20060035145A1 true US20060035145A1 (en) | 2006-02-16 |
Family
ID=34620666
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/756,015 Abandoned US20050153203A1 (en) | 2004-01-13 | 2004-01-13 | Lead-zinc battery |
US11/249,223 Abandoned US20060035145A1 (en) | 2004-01-13 | 2005-10-13 | Lead-zinc battery |
US11/763,029 Expired - Fee Related US7682737B2 (en) | 2004-01-13 | 2007-06-14 | Lead-zinc storage battery |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/756,015 Abandoned US20050153203A1 (en) | 2004-01-13 | 2004-01-13 | Lead-zinc battery |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/763,029 Expired - Fee Related US7682737B2 (en) | 2004-01-13 | 2007-06-14 | Lead-zinc storage battery |
Country Status (4)
Country | Link |
---|---|
US (3) | US20050153203A1 (en) |
EP (1) | EP1555710A1 (en) |
JP (1) | JP2005203369A (en) |
CA (1) | CA2491534A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080090147A1 (en) * | 2006-10-12 | 2008-04-17 | Stauffer John E | Tin-zinc secondary battery |
US20080183399A1 (en) * | 2003-08-01 | 2008-07-31 | Dexcom, Inc. | System and methods for processing analyte sensor data |
US20080187830A1 (en) * | 2006-10-12 | 2008-08-07 | Stauffer John E | Tin-zinc secondary battery |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7550230B2 (en) * | 2001-03-15 | 2009-06-23 | Powergenix Systems, Inc. | Electrolyte composition for nickel-zinc batteries |
US7947391B2 (en) * | 2004-01-13 | 2011-05-24 | Stauffer John E | Lead-alkaline battery |
CN100459241C (en) * | 2007-05-21 | 2009-02-04 | 赵恒祥 | Additive of accumulator positive material and modified accumlator positive material |
US8232003B2 (en) * | 2009-04-14 | 2012-07-31 | Stauffer John E | Lead-palladium battery |
JP6150383B2 (en) * | 2013-03-28 | 2017-06-21 | 日産自動車株式会社 | Electrolyte for alkaline battery and alkaline battery |
US9899695B2 (en) | 2015-05-22 | 2018-02-20 | General Electric Company | Zinc-based electrolyte compositions, and related electrochemical processes and articles |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1955115A (en) * | 1929-10-29 | 1934-04-17 | Drumm Battery Company Ltd | Storage battery |
US3862861A (en) * | 1970-08-03 | 1975-01-28 | Gates Rubber Co | Maintenance-free type lead acid |
US4830718A (en) * | 1985-10-21 | 1989-05-16 | John Stauffer | Removal of sulfur dioxide (SO2) from waste gases and recovery as sulfuric acid |
US5344529A (en) * | 1991-06-17 | 1994-09-06 | Stauffer John E | Bipolar process for removal of sulfur dioxide from waste gases |
US5512144A (en) * | 1995-03-28 | 1996-04-30 | John E. Stauffer | Pulse method for sulfur dioxide electrolysis |
US5705050A (en) * | 1996-04-29 | 1998-01-06 | Sampson; Richard L. | Electrolytic process and apparatus for the controlled oxidation and reduction of inorganic and organic species in aqueous solutions |
US6235167B1 (en) * | 1999-12-10 | 2001-05-22 | John E. Stauffer | Electrolyzer for the production of sodium chlorate |
US6391186B1 (en) * | 1998-11-30 | 2002-05-21 | John E. Stauffer | Electrochemical process for removing ions from solution |
US20030190524A1 (en) * | 2000-11-10 | 2003-10-09 | Jeffrey Phillips | Positive and negative interactive electrode formulation for a zinc-containing cell having an alkaline electrolyte |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3447971A (en) * | 1966-12-30 | 1969-06-03 | Chrysler Corp | Neutral secondary battery |
US3833427A (en) * | 1973-07-27 | 1974-09-03 | Polaroid Corp | Planar battery, process of manufacture thereof and film cassette including the same |
US3944435A (en) * | 1974-12-24 | 1976-03-16 | Union Carbide Corporation | Bonded component assembly for flat cells and method therefor |
US4076909A (en) * | 1975-09-25 | 1978-02-28 | Ab Olle Lindstrom | Alkaline lead battery |
NL7602840A (en) * | 1976-03-18 | 1977-09-20 | Lindstroem Ab Olle | Electric accumulators with lead oxide positive electrode - and iron, cadmium, magnesium, indium or zinc negative electrode |
JPS56165271A (en) * | 1980-05-23 | 1981-12-18 | Matsushita Electric Ind Co Ltd | Primary battery |
IL100903A (en) * | 1992-02-10 | 1995-06-29 | Pecherer Eugeny | Zinc anode for batteries with improved performance |
US6010604A (en) | 1998-02-04 | 2000-01-04 | Stauffer; John E. | Neural network packing |
CN1450679A (en) * | 2003-04-22 | 2003-10-22 | 陈舒 | Alkaline lead-zinc accumulator |
-
2004
- 2004-01-13 US US10/756,015 patent/US20050153203A1/en not_active Abandoned
-
2005
- 2005-01-05 CA CA002491534A patent/CA2491534A1/en not_active Abandoned
- 2005-01-07 EP EP05250057A patent/EP1555710A1/en not_active Withdrawn
- 2005-01-12 JP JP2005005271A patent/JP2005203369A/en active Pending
- 2005-10-13 US US11/249,223 patent/US20060035145A1/en not_active Abandoned
-
2007
- 2007-06-14 US US11/763,029 patent/US7682737B2/en not_active Expired - Fee Related
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1955115A (en) * | 1929-10-29 | 1934-04-17 | Drumm Battery Company Ltd | Storage battery |
US3862861A (en) * | 1970-08-03 | 1975-01-28 | Gates Rubber Co | Maintenance-free type lead acid |
US3862861B1 (en) * | 1970-08-03 | 1987-04-07 | ||
US4830718A (en) * | 1985-10-21 | 1989-05-16 | John Stauffer | Removal of sulfur dioxide (SO2) from waste gases and recovery as sulfuric acid |
US5344529A (en) * | 1991-06-17 | 1994-09-06 | Stauffer John E | Bipolar process for removal of sulfur dioxide from waste gases |
US5512144A (en) * | 1995-03-28 | 1996-04-30 | John E. Stauffer | Pulse method for sulfur dioxide electrolysis |
US5705050A (en) * | 1996-04-29 | 1998-01-06 | Sampson; Richard L. | Electrolytic process and apparatus for the controlled oxidation and reduction of inorganic and organic species in aqueous solutions |
US6391186B1 (en) * | 1998-11-30 | 2002-05-21 | John E. Stauffer | Electrochemical process for removing ions from solution |
US6235167B1 (en) * | 1999-12-10 | 2001-05-22 | John E. Stauffer | Electrolyzer for the production of sodium chlorate |
US20030190524A1 (en) * | 2000-11-10 | 2003-10-09 | Jeffrey Phillips | Positive and negative interactive electrode formulation for a zinc-containing cell having an alkaline electrolyte |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080183399A1 (en) * | 2003-08-01 | 2008-07-31 | Dexcom, Inc. | System and methods for processing analyte sensor data |
US20080090147A1 (en) * | 2006-10-12 | 2008-04-17 | Stauffer John E | Tin-zinc secondary battery |
US20080187830A1 (en) * | 2006-10-12 | 2008-08-07 | Stauffer John E | Tin-zinc secondary battery |
US7550231B2 (en) * | 2006-10-12 | 2009-06-23 | Stauffer John E | Tin-zinc secondary battery |
Also Published As
Publication number | Publication date |
---|---|
US20050153203A1 (en) | 2005-07-14 |
US20070238022A1 (en) | 2007-10-11 |
CA2491534A1 (en) | 2005-07-13 |
JP2005203369A (en) | 2005-07-28 |
US7682737B2 (en) | 2010-03-23 |
EP1555710A1 (en) | 2005-07-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Besenhard | Handbook of battery materials | |
US7608361B2 (en) | Alkali metal battery | |
US20100047697A1 (en) | Lead-zinc battery | |
WO2007002160A2 (en) | Lead-alkaline battery | |
US7682737B2 (en) | Lead-zinc storage battery | |
CN102005615A (en) | Rechargeable nickel ion battery | |
US20130045415A1 (en) | Lead-zinc battery | |
JP2004513499A (en) | Cathode formulation for low toxicity zinc electrodes with additives whose redox potential is positive with respect to zinc potential | |
JP2004520683A (en) | Cathode formulation for low toxicity zinc electrodes with additives whose redox potential is negative with respect to zinc potential | |
US9147912B2 (en) | Method of producing an electrical potential | |
JP2004522256A (en) | Zinc negative electrode formulation for rechargeable cells with alkaline electrolyte | |
US8932753B2 (en) | Lead alkaline battery | |
JP7343116B1 (en) | secondary battery | |
US20090181312A1 (en) | Lead-alkaline battery | |
US20080152999A1 (en) | Energy Converter Cell For the Direct Conversion of Radiation and/or Thermal Energy Into Electrical Energy | |
US20210408610A1 (en) | High voltage rechargeable Zn-MnO2 battery | |
US12119495B2 (en) | Electric batteries and methods for producing the same | |
TWI270227B (en) | Secondary cell | |
US20190131679A1 (en) | Energy storage device electrolyte additive | |
CN113353481B (en) | Waste battery recovery unit of leak protection liquid | |
JPS62211863A (en) | Nonaqueous electrolyte battery | |
CN101222068A (en) | Carbon zinc battery with charge-discharge function | |
CN102386433A (en) | Secondary battery | |
KR20200041213A (en) | A positive electrode containing copper oxide and dual-ion storage rechargeable batteries containing the same | |
JPS5819876A (en) | Electrolyte |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |