CA1087244A - Alloy-coated cathode for lead-acid batteries - Google Patents
Alloy-coated cathode for lead-acid batteriesInfo
- Publication number
- CA1087244A CA1087244A CA271,348A CA271348A CA1087244A CA 1087244 A CA1087244 A CA 1087244A CA 271348 A CA271348 A CA 271348A CA 1087244 A CA1087244 A CA 1087244A
- Authority
- CA
- Canada
- Prior art keywords
- antimony
- grid
- lead
- alloy
- active material
- 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.)
- Expired
Links
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 46
- 239000000956 alloy Substances 0.000 title claims abstract description 46
- 239000002253 acid Substances 0.000 title claims 2
- 229910052787 antimony Inorganic materials 0.000 claims abstract description 69
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims abstract description 64
- 229910000978 Pb alloy Inorganic materials 0.000 claims abstract description 34
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 12
- 231100000572 poisoning Toxicity 0.000 claims abstract description 12
- 230000000607 poisoning effect Effects 0.000 claims abstract description 12
- 238000003860 storage Methods 0.000 claims abstract description 11
- 150000002739 metals Chemical class 0.000 claims abstract description 9
- 239000011149 active material Substances 0.000 claims description 24
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 8
- 229910052718 tin Inorganic materials 0.000 claims description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 4
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 4
- 229910052785 arsenic Inorganic materials 0.000 claims description 4
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 4
- 229910017052 cobalt Inorganic materials 0.000 claims description 4
- 239000010941 cobalt Substances 0.000 claims description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 229910052750 molybdenum Inorganic materials 0.000 claims description 4
- 239000011733 molybdenum Substances 0.000 claims description 4
- 229910052711 selenium Inorganic materials 0.000 claims description 4
- 239000011669 selenium Substances 0.000 claims description 4
- 229910052709 silver Inorganic materials 0.000 claims description 4
- 239000004332 silver Substances 0.000 claims description 4
- 229910052714 tellurium Inorganic materials 0.000 claims description 4
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052725 zinc Inorganic materials 0.000 claims description 4
- 239000011701 zinc Substances 0.000 claims description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 3
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 claims description 3
- 238000005275 alloying Methods 0.000 claims description 3
- 229910052797 bismuth Inorganic materials 0.000 claims description 3
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 3
- 229910052793 cadmium Inorganic materials 0.000 claims description 3
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 239000011651 chromium Substances 0.000 claims description 3
- 229910052733 gallium Inorganic materials 0.000 claims description 3
- 229910052732 germanium Inorganic materials 0.000 claims description 3
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 claims description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052737 gold Inorganic materials 0.000 claims description 3
- 239000010931 gold Substances 0.000 claims description 3
- 229910052738 indium Inorganic materials 0.000 claims description 3
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 229910052716 thallium Inorganic materials 0.000 claims description 3
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 claims description 3
- 230000003334 potential effect Effects 0.000 claims description 2
- 229910001245 Sb alloy Inorganic materials 0.000 abstract description 10
- 239000002140 antimony alloy Substances 0.000 abstract description 10
- 239000011248 coating agent Substances 0.000 abstract description 5
- 238000000576 coating method Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 229940075103 antimony Drugs 0.000 description 55
- 239000010410 layer Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000000151 deposition Methods 0.000 description 4
- 230000008021 deposition Effects 0.000 description 4
- 239000001999 grid alloy Substances 0.000 description 3
- 235000016768 molybdenum Nutrition 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- 229940058905 antimony compound for treatment of leishmaniasis and trypanosomiasis Drugs 0.000 description 2
- 150000001463 antimony compounds Chemical class 0.000 description 2
- 229910000410 antimony oxide Inorganic materials 0.000 description 2
- LJCFOYOSGPHIOO-UHFFFAOYSA-N antimony pentoxide Chemical compound O=[Sb](=O)O[Sb](=O)=O LJCFOYOSGPHIOO-UHFFFAOYSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VTRUBDSFZJNXHI-UHFFFAOYSA-N oxoantimony Chemical compound [Sb]=O VTRUBDSFZJNXHI-UHFFFAOYSA-N 0.000 description 2
- RILZRCJGXSFXNE-UHFFFAOYSA-N 2-[4-(trifluoromethoxy)phenyl]ethanol Chemical compound OCCC1=CC=C(OC(F)(F)F)C=C1 RILZRCJGXSFXNE-UHFFFAOYSA-N 0.000 description 1
- 229910000531 Co alloy Inorganic materials 0.000 description 1
- PYPDMIQMPWEFHX-UHFFFAOYSA-N [Pb].[Co] Chemical compound [Pb].[Co] PYPDMIQMPWEFHX-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QCUOBSQYDGUHHT-UHFFFAOYSA-L cadmium sulfate Chemical compound [Cd+2].[O-]S([O-])(=O)=O QCUOBSQYDGUHHT-UHFFFAOYSA-L 0.000 description 1
- 229910000369 cadmium(II) sulfate Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 229910001174 tin-lead alloy Inorganic materials 0.000 description 1
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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/68—Selection of materials for use in lead-acid accumulators
- H01M4/685—Lead alloys
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
An improved grid for the production of positive electrodes for use in electric storage batteries is disclosed. The grid is formed of a base of lead or a lead alloy which is essentially antimony-free and the base is coated with a lead alloy containing one or more metals whereby the resulting grid achieves charging potentials essentially the same as achieved with conventional lead-antimony alloy grids while minimizing the possibilities of antimony poisoning. The grid may be made by electrically coating the surface alloy onto the support.
An improved grid for the production of positive electrodes for use in electric storage batteries is disclosed. The grid is formed of a base of lead or a lead alloy which is essentially antimony-free and the base is coated with a lead alloy containing one or more metals whereby the resulting grid achieves charging potentials essentially the same as achieved with conventional lead-antimony alloy grids while minimizing the possibilities of antimony poisoning. The grid may be made by electrically coating the surface alloy onto the support.
Description
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BACKGROUND OF THE INVENTION
. . ~
The present invention concerns grids for positive electrodes in electrical lead storage batteries and particularly grids made from lead alloys which are free of antimony or contain only a small amount of antimony. The invention can be applied to all types of positive lead electrodes.
Grids for lead electrodes of electrical storage batteries, both positive and negative electrodes, have been made for many years of cast lead alloys, generally containing 6 to 12 per cent antimony. While the antimony has been added primarily to improve the mechanical properties of the grid, it has also affected the physical structure and the electrochemical conditions in the battery cells. The antimony added to the grid alloy has contributed many advantages but it has also resulted in the important disadvantage of the so-called antimony poisoning of the negative electrode.
In order to counteract antimony poisoning, electrode grids have been produced of an antimony-free lead alloy and such grids have been used in lead storage batteries either solely for the negative electrodes or for both the positive and negative elect-rode. Since antimony migrates through the electrolyte from the positive electrode to the negative electrode, it has been proven insufficient tc construct the grid for only the negative elect-rode from antimony-free lead alloys. There has therefore been an effort to make all electrode grids from antimony-free alloys and batteries incorporating such grids are produced to a limited extent. The absence of antimony from grid alloys, however, has led to other problems. There have been attempts to counter .
BACKGROUND OF THE INVENTION
. . ~
The present invention concerns grids for positive electrodes in electrical lead storage batteries and particularly grids made from lead alloys which are free of antimony or contain only a small amount of antimony. The invention can be applied to all types of positive lead electrodes.
Grids for lead electrodes of electrical storage batteries, both positive and negative electrodes, have been made for many years of cast lead alloys, generally containing 6 to 12 per cent antimony. While the antimony has been added primarily to improve the mechanical properties of the grid, it has also affected the physical structure and the electrochemical conditions in the battery cells. The antimony added to the grid alloy has contributed many advantages but it has also resulted in the important disadvantage of the so-called antimony poisoning of the negative electrode.
In order to counteract antimony poisoning, electrode grids have been produced of an antimony-free lead alloy and such grids have been used in lead storage batteries either solely for the negative electrodes or for both the positive and negative elect-rode. Since antimony migrates through the electrolyte from the positive electrode to the negative electrode, it has been proven insufficient tc construct the grid for only the negative elect-rode from antimony-free lead alloys. There has therefore been an effort to make all electrode grids from antimony-free alloys and batteries incorporating such grids are produced to a limited extent. The absence of antimony from grid alloys, however, has led to other problems. There have been attempts to counter .
-2-i 7;2 4~
these problems in various ways, for example, by mixing antimony compounds in the active mass of the electrodes, or by making the electrode grid from alloys containing a small quantity of anti-mony. It has been found, though, that in order to avoid the dis-advantages which are connected with antimony-free alloys, the amount of antimony in the alloys had to approach 3 to 5 percent by weight. At this level of antimony content, however, antimony poisoning of the negative electrode still occurs, even though its effect may appear after a longer time and be less powerful than at the more conventional higher levels of antimony content.
The use of antimony-free alloys at the boundary layer between grid and active material can give rise to conditions which can, among other things, cause high charging potential at the electrode grid, at least in the beginning of the charging process. The application of a thin outer layer of pure antimony to antimony-free grids has therefore been tried. Investigations have shown, however, that such grids show approximately the same high charging potential as antimony-free grids under the same conditions. It has been determined, therefore, that none of the above-mentioned methods for avoiding the effects which appear, for example, as high charging potentials have led to the desired results.
It has also been proposed, see U.S. Patent 2,282,760, to form the grid of a base or support made of a conventional lead alloy obtaining a relatively high antimony content (e.g., 12 or 13 weight percent antimony, balance lead) and to coat the support with a lead alloy containing less than 0.5 (generally less than about 0.2) weight percent antimony. The absence of antimony from the grid surfaces in contact with the active material has led to other problems, however, and the use of such construction has not proven commercially attractive.
these problems in various ways, for example, by mixing antimony compounds in the active mass of the electrodes, or by making the electrode grid from alloys containing a small quantity of anti-mony. It has been found, though, that in order to avoid the dis-advantages which are connected with antimony-free alloys, the amount of antimony in the alloys had to approach 3 to 5 percent by weight. At this level of antimony content, however, antimony poisoning of the negative electrode still occurs, even though its effect may appear after a longer time and be less powerful than at the more conventional higher levels of antimony content.
The use of antimony-free alloys at the boundary layer between grid and active material can give rise to conditions which can, among other things, cause high charging potential at the electrode grid, at least in the beginning of the charging process. The application of a thin outer layer of pure antimony to antimony-free grids has therefore been tried. Investigations have shown, however, that such grids show approximately the same high charging potential as antimony-free grids under the same conditions. It has been determined, therefore, that none of the above-mentioned methods for avoiding the effects which appear, for example, as high charging potentials have led to the desired results.
It has also been proposed, see U.S. Patent 2,282,760, to form the grid of a base or support made of a conventional lead alloy obtaining a relatively high antimony content (e.g., 12 or 13 weight percent antimony, balance lead) and to coat the support with a lead alloy containing less than 0.5 (generally less than about 0.2) weight percent antimony. The absence of antimony from the grid surfaces in contact with the active material has led to other problems, however, and the use of such construction has not proven commercially attractive.
-3-; - .
- , 10~7244 OBJECTS AND SUMMARY OF THE INVENTION
It is an object of this invention to avoid or alleviate the problems of the prior ar-t.
It is also an object of this invention to provide a grid for a positive electrode for an electric storage battery and a method for producing such grid.
It is further an object of this invention to provide a grid for a positive electrode for an electric storage battery which minimizes the problems associated with antimony poisoning while providing charging potentials comparable with those provided by conventional lead-antimony grids.
The present invention provides a grid which combines the advantages of a grid alloy containing little or no antimony with the conditions at the boundary layer between the grid and the active material which are obtained with conventional antimony alloys. The invention also includes a method for producing such grids.
In accordance with one aspect of the present invention, there is provided a grid for a positive electrode for electrical storage battery also including a negative electrode comprising a base of lead or a lead alloy which is essentially free from antimony coated on at least all surfaces which contact active material in the finished electrode with a lead alloy of a different composition, the alloying metals of the surface layer being chosen such that the resulting grid achieves charging potentials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode.
' : , ' , - 1~87244 Another aspect of the present invention provides a method of producing grids for positive electrodes for an electric storage battery, which grids comprise lead or a lead alloy which is essentially free from antimony coated with a lead surface alloy of another composition, the alloying metals of the surface layer being chosen such that the resulting grid achieves charging potentials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode, which comprises applying the surface alloy by an electrolytic process.
DESCRIPTION OF THE DRAWINGS
FIGURE 1 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of a conventional lead-antimony alloy.
FIGURE 2 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy.
FIGURE 3 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a layer of pure antimony.
FIGURE 4 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy where antimony oxide is included in the active material.
. , ~ , 7Z4~
FIGURE 5 is a graph of the present invention with a base of an antimony-free lead alloy coated with a lead surface alloy lf 12 micrometers thickness containing 10 to 15 weight percent antimony.
FIGURE 6 is a graph of the present invention with a base of an antimony-free lead alloy coated with a lead surface alloy of 20 micrometers thickness containing 10 to 15 weight percent antimony.
FIGURE 7 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a tin-lead alloy.
FIGURE 8 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a cobalt-lead alloy.
DETAILED DESCRIPTION OF THE INVENTION
According to the present invention, grids for the positive electrodes of electric storage batteries are made of lead or of a lead alloy which is essentially free from antimony that is, a lead alloy which contains none or only a little antimony (3 weight percent maximum). The grid is coated on its surface with a lead alloy of a different composition than the base composition. The surface alloy contains from 3 to 95 weight percent of one or more of the metals copper, silver, gold, zinc, cadmium, germanium, indium, thallium, gallium, tin, arsenic, antimony, bismuth, selenium, tellurium, chromium/ moly-bdenum, nickel, and cobalt. It has been found that with the choice of the proper surface alloy, the same charging potential can be achieved with grids made according to the present inven-tion as with conventional lead-antimony grids. Charging poten-tials are essentially less than those obtained with grids ofthe antimony-free or low-antimony type. The surface alloy can contain one or more of the above-named metals, although ~ $
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copper, silver, zinc, tin, arsenic, antimony, selenium, tellurium, molybdenum, and cobalt are preferred for economic and other reasons. Especially suitable is ~ 6a-*, ,.
~, .'' ~
.
an alloy containing from about 3 to 95, preferably from about 5 to 25 percent, by weight antimony, balance essentially lead.
Tin is also suitable for inclusion in the lead-antimony surface alloy. When antimony is utilized in the surface alloy, the risk of antimony poisoning of the negative electrodes must be con-sidered at the same time as the desired creation of the boundary conditions between the grid and the active material which cor-respond to the conditions which are obtained with a homogeneous lead-antimony alloy for the grid. As the electrode utilizing a grid of the present invention with an antimony-containing coat-ing is charged and discharged, corrosion of the grid takes place, by means of which the amount of active material is increased.
Through this mechanism the positive active material gains antimony from the outer layer of the positive grid. The amount of antimony in the surface alloy should therefore be chosen so that eventual antimony poisoning of the negative electrode can be avoided. The active material in the positive electrode, however, has a certain capacity or tendency to absorb antimony. Although the maximum amount of antimony which may be absorbed without antimony poisoning has not been determined, the antimony content should not be greater than about 2 percent by weight of the active material.
Preferably, the total amount of antimony in the surface alloy should be chosen so that it is less than 1, preferably about 0.5, percent by weight of the active material. The thickness of the surface alloy is generally from about 5 to 25, preferably from about 10 to 20, microns.
The invention is additionally illustrated in connection with the following Example which is to be considered as illustrative of the present invention. It should be understood, however, that the invention is not limited to the specific details of the Example.
`
10~7Z44 E X A M P L E
Test electrodes of the so-called tubular type were built with various types of grids. After charging and dischar-ging the electrodes, the charging potential was measured against a reference electrode of the CdSO4/Cd type. The charging current was 10 milliamperes per gram of active material. The results obtained are shown in the diagrams of Figures 1 to 6, which show the potential as a function of time during charging. Figure 1 relates to an electrode with grid of conventional lead-antimony alloy. Figure 2 relates to an electrode with grid of antimony-free lead alloy without any surface alloy or mixture of antimony compounds in the active material. The charging potentials may be seen to be noticeably higher for antimony-free alloy than for the antimony alloy.
It should be mentioned that the tests were carried out under conditions which accentuated the differences in charging potential. Under other conditions the differences would be smaller. The test conditions were chosen, however, so that they correspond to actual operational conditions. Figure 3 shows the charging potential from an electrode with grid of antimony-free alloy which was coated with a surface layer of pure antimony to a thickness of 12 micrometers. This may be ~
seen to favorably affect the charging potential without, how- ~ -ever, reaching the low values obtained with the conventional lead-antimony alloy. Tests were also made with thinner layers of antimony, which gave, however, a further worsening of the results. Figure 4 shows another case of known technique, namely the mixing of antimony oxide in the active material.
In this case 0.5 percent by weight of antimony pentoxide was added. The grid of the electrode was C
1~872~4 of an antimony-free lead alloy, without surface coating. The potential values obtained agree well with those obtained without additives to the active material. Figure 5 shows the result obtained with electrodes which are provided with grids according to the invention. In this case the grid is of antimony-free alloy and coated with a surface alloy which contained 10 to 15 weight percent antimony and had a thickness of 12 micrometers. A
noticeable decrease of charging potential is obtained, although the values obtained are negligibly greater than those obtained with the conventional lead-antimony alloy. The same experiment was carried out with a layer thickness of 20 micrometers (Figure 6) and results were obtained which essentially completely agree with those obtained with conventional lead-antimony alloys.
Similar results are also obtained using alloys of lead and one or more of metals copper, silver, gold, zinc, cadmium, germanium, indium, thallium, gallium, tin, arsenic, bismuth, selenium, tellurium, chromium, molybdenum, nickel and cobalt.
Several different methods may be utilized for applying the surface alloy including electroplating, dipping in molten alloy, spray metallization, as well as deposition of evaporated metal in a vacuum. Electroplating is preferred. It is theoretically conceivable to deposit the alloy from an electrolytic bath. The metals which are to be deposited together should preferably have the same deposition potential, i.e., cathodic potential.
Important factors in this regard are metal ion concentration, temperature, current density, pH, and others. If it is desired to simultaneously deposit metals which have greatly differing deposition potentials, the proper conditions can be acheived by -adding materials to the bath whichform complexes with one of `: ~
1~72~
the metal species. In the Example above, the lead-antimony surface coating for the grid of the present invention was applied from a fluoroborate, and fluoroboric acid and small quantities of organic additive agents. Current density at deposition was 2 to
- , 10~7244 OBJECTS AND SUMMARY OF THE INVENTION
It is an object of this invention to avoid or alleviate the problems of the prior ar-t.
It is also an object of this invention to provide a grid for a positive electrode for an electric storage battery and a method for producing such grid.
It is further an object of this invention to provide a grid for a positive electrode for an electric storage battery which minimizes the problems associated with antimony poisoning while providing charging potentials comparable with those provided by conventional lead-antimony grids.
The present invention provides a grid which combines the advantages of a grid alloy containing little or no antimony with the conditions at the boundary layer between the grid and the active material which are obtained with conventional antimony alloys. The invention also includes a method for producing such grids.
In accordance with one aspect of the present invention, there is provided a grid for a positive electrode for electrical storage battery also including a negative electrode comprising a base of lead or a lead alloy which is essentially free from antimony coated on at least all surfaces which contact active material in the finished electrode with a lead alloy of a different composition, the alloying metals of the surface layer being chosen such that the resulting grid achieves charging potentials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode.
' : , ' , - 1~87244 Another aspect of the present invention provides a method of producing grids for positive electrodes for an electric storage battery, which grids comprise lead or a lead alloy which is essentially free from antimony coated with a lead surface alloy of another composition, the alloying metals of the surface layer being chosen such that the resulting grid achieves charging potentials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode, which comprises applying the surface alloy by an electrolytic process.
DESCRIPTION OF THE DRAWINGS
FIGURE 1 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of a conventional lead-antimony alloy.
FIGURE 2 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy.
FIGURE 3 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a layer of pure antimony.
FIGURE 4 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy where antimony oxide is included in the active material.
. , ~ , 7Z4~
FIGURE 5 is a graph of the present invention with a base of an antimony-free lead alloy coated with a lead surface alloy lf 12 micrometers thickness containing 10 to 15 weight percent antimony.
FIGURE 6 is a graph of the present invention with a base of an antimony-free lead alloy coated with a lead surface alloy of 20 micrometers thickness containing 10 to 15 weight percent antimony.
FIGURE 7 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a tin-lead alloy.
FIGURE 8 is a graph of the charging potential (voltage) as a function of time for an electrode made with a grid of an antimony-free lead alloy coated with a cobalt-lead alloy.
DETAILED DESCRIPTION OF THE INVENTION
According to the present invention, grids for the positive electrodes of electric storage batteries are made of lead or of a lead alloy which is essentially free from antimony that is, a lead alloy which contains none or only a little antimony (3 weight percent maximum). The grid is coated on its surface with a lead alloy of a different composition than the base composition. The surface alloy contains from 3 to 95 weight percent of one or more of the metals copper, silver, gold, zinc, cadmium, germanium, indium, thallium, gallium, tin, arsenic, antimony, bismuth, selenium, tellurium, chromium/ moly-bdenum, nickel, and cobalt. It has been found that with the choice of the proper surface alloy, the same charging potential can be achieved with grids made according to the present inven-tion as with conventional lead-antimony grids. Charging poten-tials are essentially less than those obtained with grids ofthe antimony-free or low-antimony type. The surface alloy can contain one or more of the above-named metals, although ~ $
~7Z4~
copper, silver, zinc, tin, arsenic, antimony, selenium, tellurium, molybdenum, and cobalt are preferred for economic and other reasons. Especially suitable is ~ 6a-*, ,.
~, .'' ~
.
an alloy containing from about 3 to 95, preferably from about 5 to 25 percent, by weight antimony, balance essentially lead.
Tin is also suitable for inclusion in the lead-antimony surface alloy. When antimony is utilized in the surface alloy, the risk of antimony poisoning of the negative electrodes must be con-sidered at the same time as the desired creation of the boundary conditions between the grid and the active material which cor-respond to the conditions which are obtained with a homogeneous lead-antimony alloy for the grid. As the electrode utilizing a grid of the present invention with an antimony-containing coat-ing is charged and discharged, corrosion of the grid takes place, by means of which the amount of active material is increased.
Through this mechanism the positive active material gains antimony from the outer layer of the positive grid. The amount of antimony in the surface alloy should therefore be chosen so that eventual antimony poisoning of the negative electrode can be avoided. The active material in the positive electrode, however, has a certain capacity or tendency to absorb antimony. Although the maximum amount of antimony which may be absorbed without antimony poisoning has not been determined, the antimony content should not be greater than about 2 percent by weight of the active material.
Preferably, the total amount of antimony in the surface alloy should be chosen so that it is less than 1, preferably about 0.5, percent by weight of the active material. The thickness of the surface alloy is generally from about 5 to 25, preferably from about 10 to 20, microns.
The invention is additionally illustrated in connection with the following Example which is to be considered as illustrative of the present invention. It should be understood, however, that the invention is not limited to the specific details of the Example.
`
10~7Z44 E X A M P L E
Test electrodes of the so-called tubular type were built with various types of grids. After charging and dischar-ging the electrodes, the charging potential was measured against a reference electrode of the CdSO4/Cd type. The charging current was 10 milliamperes per gram of active material. The results obtained are shown in the diagrams of Figures 1 to 6, which show the potential as a function of time during charging. Figure 1 relates to an electrode with grid of conventional lead-antimony alloy. Figure 2 relates to an electrode with grid of antimony-free lead alloy without any surface alloy or mixture of antimony compounds in the active material. The charging potentials may be seen to be noticeably higher for antimony-free alloy than for the antimony alloy.
It should be mentioned that the tests were carried out under conditions which accentuated the differences in charging potential. Under other conditions the differences would be smaller. The test conditions were chosen, however, so that they correspond to actual operational conditions. Figure 3 shows the charging potential from an electrode with grid of antimony-free alloy which was coated with a surface layer of pure antimony to a thickness of 12 micrometers. This may be ~
seen to favorably affect the charging potential without, how- ~ -ever, reaching the low values obtained with the conventional lead-antimony alloy. Tests were also made with thinner layers of antimony, which gave, however, a further worsening of the results. Figure 4 shows another case of known technique, namely the mixing of antimony oxide in the active material.
In this case 0.5 percent by weight of antimony pentoxide was added. The grid of the electrode was C
1~872~4 of an antimony-free lead alloy, without surface coating. The potential values obtained agree well with those obtained without additives to the active material. Figure 5 shows the result obtained with electrodes which are provided with grids according to the invention. In this case the grid is of antimony-free alloy and coated with a surface alloy which contained 10 to 15 weight percent antimony and had a thickness of 12 micrometers. A
noticeable decrease of charging potential is obtained, although the values obtained are negligibly greater than those obtained with the conventional lead-antimony alloy. The same experiment was carried out with a layer thickness of 20 micrometers (Figure 6) and results were obtained which essentially completely agree with those obtained with conventional lead-antimony alloys.
Similar results are also obtained using alloys of lead and one or more of metals copper, silver, gold, zinc, cadmium, germanium, indium, thallium, gallium, tin, arsenic, bismuth, selenium, tellurium, chromium, molybdenum, nickel and cobalt.
Several different methods may be utilized for applying the surface alloy including electroplating, dipping in molten alloy, spray metallization, as well as deposition of evaporated metal in a vacuum. Electroplating is preferred. It is theoretically conceivable to deposit the alloy from an electrolytic bath. The metals which are to be deposited together should preferably have the same deposition potential, i.e., cathodic potential.
Important factors in this regard are metal ion concentration, temperature, current density, pH, and others. If it is desired to simultaneously deposit metals which have greatly differing deposition potentials, the proper conditions can be acheived by -adding materials to the bath whichform complexes with one of `: ~
1~72~
the metal species. In the Example above, the lead-antimony surface coating for the grid of the present invention was applied from a fluoroborate, and fluoroboric acid and small quantities of organic additive agents. Current density at deposition was 2 to
4 amperes per dm2 grid area.
The use of an electrolytic process for applying the surface alloy also allows control of the particular surface of the grid to be coated with surface alloy. In many cases it is desirable to coat only those surfaces which are in direct contact with active material. The electrolytic method is also very suitable for treatment of those grids which are made from drawn or cast lead wire. In this instance, the coating of the wire can proceed in a continuous process in connection with the production of the wire.
A large number of alloys may be utilized as the surface alloy for electrode grids according to the present invention.
It is important, however, that the alloy contain lead to the extent that a material structure can be created which in its properties is similar to that obtained from the conventional lead-antimony alloys.
The principles, preferred embodiments and modes of operation of the present invention have been described in the foregoing specification. The invention which is intended to be protected herein, however, is not to be construed as limited to the particular forms disclosed, since these are to be regarded as illustrative rather than restrictive. Variations and changes may be made by those skilled in the art without departing from the spirit of the invention.
~ '.
~' :
~-` i 10~7Z44 -E~ample 2 Test cells were built with grid made from an antimony free lead alloy, having a surface alloy comprising lead and tin, The electrodes were of the tubular type having an inner tube diameter of 8.3 mm, The grid spine~ had a diameter of 3.5 mm and were cast from an alloy compri~ing As-0,05 ~J~ Te-0.04 ~o Ag-0,01 ,', the rest being lead with the usual small amonts of contaminants. The surface alloy had 18 % tin, the rest being lead. It ~as applied in a layer of 20,'~ thickness. The electrodes were discharged several times v~ith currents between 5 and 10 mA
per gram of active material, After each discharge the electrodes were charged with a constant current of approximately 10 mA/gram of active material. The charging potential was measured against the reference electrode as in example 1. Figur 7 shows the potential a~q function of charging time as measured ~hen charging the electrode after the third discharge.
Example 3 Electrode3 were made in the same way as in example 2, but with the surface alloy having a thickness of 12,~ and comprising about ~.5 ~o Co. The surface alloy wa9 applied as two layers of pure lead snd two layers of a lead 7 ~o Co alloy. After charging and dis-charging under the same conditions as given in example 2, the chargin~ potential as function of time was recorded as illustrated by figur 8.
-lOa-.
` ~' ' - ' ''' !
`- ` ;
The use of an electrolytic process for applying the surface alloy also allows control of the particular surface of the grid to be coated with surface alloy. In many cases it is desirable to coat only those surfaces which are in direct contact with active material. The electrolytic method is also very suitable for treatment of those grids which are made from drawn or cast lead wire. In this instance, the coating of the wire can proceed in a continuous process in connection with the production of the wire.
A large number of alloys may be utilized as the surface alloy for electrode grids according to the present invention.
It is important, however, that the alloy contain lead to the extent that a material structure can be created which in its properties is similar to that obtained from the conventional lead-antimony alloys.
The principles, preferred embodiments and modes of operation of the present invention have been described in the foregoing specification. The invention which is intended to be protected herein, however, is not to be construed as limited to the particular forms disclosed, since these are to be regarded as illustrative rather than restrictive. Variations and changes may be made by those skilled in the art without departing from the spirit of the invention.
~ '.
~' :
~-` i 10~7Z44 -E~ample 2 Test cells were built with grid made from an antimony free lead alloy, having a surface alloy comprising lead and tin, The electrodes were of the tubular type having an inner tube diameter of 8.3 mm, The grid spine~ had a diameter of 3.5 mm and were cast from an alloy compri~ing As-0,05 ~J~ Te-0.04 ~o Ag-0,01 ,', the rest being lead with the usual small amonts of contaminants. The surface alloy had 18 % tin, the rest being lead. It ~as applied in a layer of 20,'~ thickness. The electrodes were discharged several times v~ith currents between 5 and 10 mA
per gram of active material, After each discharge the electrodes were charged with a constant current of approximately 10 mA/gram of active material. The charging potential was measured against the reference electrode as in example 1. Figur 7 shows the potential a~q function of charging time as measured ~hen charging the electrode after the third discharge.
Example 3 Electrode3 were made in the same way as in example 2, but with the surface alloy having a thickness of 12,~ and comprising about ~.5 ~o Co. The surface alloy wa9 applied as two layers of pure lead snd two layers of a lead 7 ~o Co alloy. After charging and dis-charging under the same conditions as given in example 2, the chargin~ potential as function of time was recorded as illustrated by figur 8.
-lOa-.
` ~' ' - ' ''' !
`- ` ;
Claims (10)
1. A grid for a positive electrode for electrical storage battery also including a negative electrode comprising a base of lead or a lead alloy which is essentially free from antimony coated on at least all surfaces which contact active material in the finished electrode with an alloy of lead and from 3 to 95 percent antimony, the amount of antimony being 2 percent or less by weight of the active material utilized in the finished electrode whereby the resulting grid achieves charging potentials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode.
2. The grid of claim 1, whereby the surface alloy contains from 5 to 25 percent antimony.
3. The grid of claim 1, whereby the surface alloy also contains at least one further alloying metal.
4. The grid of claim 3, whereby the lead surface alloy further contains one or more of the metals selected from the group consisting of copper, silver, gold, zinc, cadmium, germanium, indium, thallium, gallium, tin, arsenic, bismuth, selenium, tellurium, chromium, molybdenum, nickel, and cobalt.
5. The grid of claim 3, whereby the surface alloy also contains tin.
6. The grid of claim 1, whereby the surface alloy contains antimony in a quantity which amounts to 0.5 percent or less by weight of the active material.
7. The grid of claim 1, whereby the surface alloy layer has a thickness of from about 2 to 25 micrometers.
8. The grid of claim 1, whereby those surfaces which come into contact with active material are coated with the said surface alloy while the remaining surfaces are partially or wholly uncoated.
9. A lead-acid storage battery having a grid for a positive electrode comprising a base of lead or a lead alloy which is essentially free from antimony coated on at least all surfaces which contact active material in the finished electrode with an alloy of lead and from 3 to 95 per-cent antimony, the amount of antimony being 2 percent or less by weight of the active material utilized in the finished electrode whereby the resulting grid achieves charging poten-tials of the same magnitude as those achieved with grids formed of lead alloys containing 6 to 12 weight percent antimony while minimizing the possibility of antimony poisoning of a negative electrode.
10. The battery of claim 9, wherein the surface alloy of the grid contains antimony in a quantity which amounts to 0.5 percent or less by weight of the active material.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE7602595-6 | 1976-02-27 | ||
| SE7602595A SE397155B (en) | 1976-02-27 | 1976-02-27 | GRAY FOR POSITIVE ELECTROD TO ELECTRIC LEAD ACCUMULATOR |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1087244A true CA1087244A (en) | 1980-10-07 |
Family
ID=20327144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA271,348A Expired CA1087244A (en) | 1976-02-27 | 1977-02-08 | Alloy-coated cathode for lead-acid batteries |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US4107407A (en) |
| CA (1) | CA1087244A (en) |
| DE (1) | DE2708351A1 (en) |
| FR (1) | FR2342562A1 (en) |
| GB (1) | GB1523092A (en) |
| SE (1) | SE397155B (en) |
Families Citing this family (33)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3211386A1 (en) * | 1982-03-27 | 1983-09-29 | Battelle-Institut E.V., 6000 Frankfurt | Active mass for use in the positive grid of lead storage batteries |
| WO1986003343A1 (en) * | 1984-11-19 | 1986-06-05 | Revere Copper And Brass Incorporated | Laminated lead alloy strip for battery grid application and electrochemical cells utilizing same |
| EP0213203B1 (en) * | 1985-02-26 | 1990-05-16 | Matsushita Electric Industrial Co., Ltd. | Grid for lead storage batteries and a method of producing the same |
| US4805277A (en) * | 1986-06-05 | 1989-02-21 | Matsushita Electric Industrial Co., Ltd. | Process for producing a grid for use in lead acid batteries |
| US4939051A (en) * | 1986-06-05 | 1990-07-03 | Matsushita Electric Industrial Co., Ltd. | Grid for use in lead acid batteries and process for producing same |
| JPS6396299A (en) * | 1986-10-13 | 1988-04-27 | Yoshizawa Kiko Toubu Kk | Insoluble anode made of lead alloy |
| US4906540A (en) * | 1989-06-15 | 1990-03-06 | Matsushita Electric Industrial Co., Ltd. | Lead-acid battery having a grid base of a lead-calcium alloy and a layer of lead-antimony-stannum alloy roll-bonded to the grid base |
| JPH04286866A (en) * | 1991-03-18 | 1992-10-12 | Matsushita Electric Ind Co Ltd | sealed lead acid battery |
| US5411821A (en) * | 1993-06-10 | 1995-05-02 | Derafe, Ltd. | Integral battery electrode structure for lead/acid batteries |
| EP0834946B1 (en) * | 1996-10-02 | 2002-09-11 | Japan Storage Battery Company Limited | Valve regulated type lead-acid battery and producing method thereof |
| ES2127124B1 (en) * | 1997-01-22 | 2000-01-01 | Tudor Acumulador | POSITIVE ELECTRODE AND LEAD ACCUMULATOR SPECIAL FOR USE IN HIGH TEMPERATURES. |
| US6274274B1 (en) | 1999-07-09 | 2001-08-14 | Johnson Controls Technology Company | Modification of the shape/surface finish of battery grid wires to improve paste adhesion |
| JP2002093457A (en) * | 2000-07-12 | 2002-03-29 | Japan Storage Battery Co Ltd | Lead storage battery |
| US6953641B2 (en) | 2001-01-05 | 2005-10-11 | Johnson Controls Technology Company | Battery grid |
| US7223499B2 (en) * | 2001-11-06 | 2007-05-29 | Gs Yuasa Corporation | Lead battery |
| KR101068378B1 (en) * | 2004-04-28 | 2011-09-28 | 파나소닉 주식회사 | Lead acid battery |
| US20060216595A1 (en) * | 2005-03-22 | 2006-09-28 | Holliday Rex W | Battery assembly having improved lug profile |
| EP3035422B1 (en) | 2005-05-23 | 2019-02-20 | Johnson Controls Technology Company | Battery grid |
| RU2477549C2 (en) | 2007-03-02 | 2013-03-10 | Джонсон Кэнтрэулз Текнолэджи Кампэни | Accumulator negative grid manufacture method |
| EP2433322A4 (en) * | 2009-05-19 | 2015-11-04 | East Penn Mfg Co | Composite current collector and methods therefor |
| MX338843B (en) | 2010-03-03 | 2016-05-03 | Johnson Controls Tech Co | Battery grids and methods for manufacturing same. |
| US9748578B2 (en) | 2010-04-14 | 2017-08-29 | Johnson Controls Technology Company | Battery and battery plate assembly |
| KR101831423B1 (en) | 2010-04-14 | 2018-02-22 | 존슨 컨트롤스 테크놀러지 컴퍼니 | Battery, battery plate assembly, and method of assembly |
| US9761883B2 (en) | 2011-11-03 | 2017-09-12 | Johnson Controls Technology Company | Battery grid with varied corrosion resistance |
| US8927143B2 (en) * | 2011-12-06 | 2015-01-06 | John E. Stauffer | Aluminum storage battery |
| US20140072868A1 (en) * | 2012-05-11 | 2014-03-13 | East Penn Manufacturing Co., | Composite Current Collector and Methods Therefor |
| DE202013012569U1 (en) | 2013-10-08 | 2017-07-17 | Johnson Controls Autobatterie Gmbh & Co. Kgaa | Grid arrangement for a plate-shaped battery electrode of an electrochemical accumulator and accumulator |
| DE102013111667A1 (en) | 2013-10-23 | 2015-04-23 | Johnson Controls Autobatterie Gmbh & Co. Kgaa | Grid arrangement for a plate-shaped battery electrode and accumulator |
| US9923242B2 (en) | 2014-01-23 | 2018-03-20 | John E. Stauffer | Lithium bromide battery |
| US9666898B2 (en) | 2014-07-22 | 2017-05-30 | John E. Stauffer | Storage battery using a uniform mix of conductive and nonconductive granules in a lithium bromide electrolyte |
| US9509017B2 (en) | 2014-07-22 | 2016-11-29 | John E. Stauffer | Lithium storage battery |
| US12451493B2 (en) | 2017-01-27 | 2025-10-21 | Cps Technology Holdings Llc | Battery grid |
| CN108682866B (en) * | 2018-04-13 | 2021-04-20 | 安徽力普拉斯电源技术有限公司 | New lead-calcium-tin-aluminum alloy, positive plate grid and lead-acid battery containing the same |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3881953A (en) * | 1973-11-26 | 1975-05-06 | St Joe Minerals Corp | Battery electrode grids and method of making same from a lead-calcium-lithium-tin alloy |
| FR542504A (en) * | 1921-10-19 | 1922-08-16 | Manufacturing process for lead-acid batteries | |
| GB649053A (en) * | 1948-05-10 | 1951-01-17 | Margaret Allen | Improvements in or relating to electrical storage batteries |
| GB1329974A (en) * | 1969-12-11 | 1973-09-12 | Electric Power Storage Ltd | Electric storage batteries |
| US3933524A (en) * | 1972-05-24 | 1976-01-20 | General Motors Corporation | Antimony plating of lead-acid storage batteries grids |
| IT989422B (en) * | 1973-06-25 | 1975-05-20 | Oronzio De Nora Impianti | CATHODE FOR USE IN ELECTROLYTIC CELLS FORMED BY NEW CATHODE MATERIALS AND METHOD FOR ITS PREPARATION |
-
1976
- 1976-02-27 SE SE7602595A patent/SE397155B/en unknown
-
1977
- 1977-02-08 CA CA271,348A patent/CA1087244A/en not_active Expired
- 1977-02-09 GB GB5340/77A patent/GB1523092A/en not_active Expired
- 1977-02-24 DE DE19772708351 patent/DE2708351A1/en not_active Withdrawn
- 1977-02-25 US US05/771,975 patent/US4107407A/en not_active Expired - Lifetime
- 1977-02-25 FR FR7705702A patent/FR2342562A1/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| GB1523092A (en) | 1978-08-31 |
| FR2342562B1 (en) | 1980-10-17 |
| FR2342562A1 (en) | 1977-09-23 |
| US4107407A (en) | 1978-08-15 |
| DE2708351A1 (en) | 1977-09-01 |
| SE397155B (en) | 1977-10-17 |
| SE7602595L (en) | 1977-08-28 |
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| MKEX | Expiry | ||
| MKEX | Expiry |
Effective date: 19971007 |