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US2619437A - Primary cells - Google Patents

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US2619437A
US2619437A US28468A US2846848A US2619437A US 2619437 A US2619437 A US 2619437A US 28468 A US28468 A US 28468A US 2846848 A US2846848 A US 2846848A US 2619437 A US2619437 A US 2619437A
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Prior art keywords
lead
cell
anode
sulphate
electrolytic solution
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US28468A
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Glasstone Samuel
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Zenith Electronics LLC
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Zenith Radio Corp
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/04Cells with aqueous electrolyte
    • H01M6/045Cells with aqueous electrolyte characterised by aqueous electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/06Lead-acid accumulators
    • H01M10/08Selection of materials as electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/04Cells with aqueous electrolyte
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • This invention relates to electrolytic apparatus, such as primary cells, apparatusincluding electrolytic baths and the like; It is a primary-object of the present invention to provide improved, apparatus of this type.
  • Yet a further object of the invention is to provide an improved primary cell of this type which is characterized by a substantially higher terminal voltage than that of' a conventional Leclanch cell.
  • Still a further object of the invention is to provide an improved primary cell which is capable of supplying large current output without I believed to be novel are set forth with particularity in the appended claim.
  • the invention, to gether with further objects and advantages thereof, may more readily be understood, however, by reference to the following description taken in connection with the accompanying drawing, in which: V
  • Figure 1 is across sectionalview ofone embodiment of the present invention.
  • Figure 2 is a cross sectional view of an alternative form of the embodiment shown in Figure 1-.
  • the anode that electrode at which metal tends to pass into solution as ions is referred to as the anode; the other electrode is referred to as the cathode.
  • the polarity of the electrodes is conventionally referred to in connection wit-h the direction of current flow in the external circuit, the direction of current flow in the external circuit being from positive to negative.
  • the anode as defined above is referred to as the negative electrode, andthe cathode as the positive electrode.
  • a primary cell l which includes a positive electrode or cathode comprising a case 2 of conductive material, such as lead; alternatively, case 2 may comprise lead or carbon deposited on the inner surface of a non-conductive material such as a plastic.
  • case 2 may comprise lead or carbon deposited on the inner surface of a non-conductive material such as a plastic.
  • an inner container 4 of porous chemically inert material may be provided to permit diffusion of electrolyte throughout the cell and to separate the mixture 3 from the inner electrode.
  • the inner container 4 may be made of porous earthenware or woven glass.
  • Chemically inert material 5 having large absorption capacity, may be packed into container 4 so as to provide means for retaining relatively large quantities of the electrolytic solution; such material may be, for example, glass Wool.
  • the negative electrode or anode 6 is of lead, preferably amalgamated and supported in the inert material 5 so as to be in contact with the electrolytic solution.
  • the cell I may be hermetically sealed by a layer 1 of wax or pitch, which layer may also aid insupporting the negative electrodefi.
  • The. electrolytic solution includes sulphuric acid, and, in accordance with the present invention, a surface active agent composed of one or more-non-polarlong chain groups associated with a polar grouping consisting of one or more polar groups and substantially resistant to deterioration by sulphuric acid.
  • the surface active agent may be dodcylbenzene sodium sulfonate.
  • surface active agents which may be used are, for example, isopropyl naphthalene sodium sulfonate, sodium lauryl sulfate, sodium myristyl sulfate, and the alkyl phenoxypolyethoxyethanols, such as methyl phenoxypolyethoxyethanol.
  • volume efficiency of the cell may be increased by the use of a saturated solution of a sulphate of an alkali metal or ammonium in the sulphuric acid electrolyte, together with an excess of solid sulphate to maintain saturation during cell discharge.
  • a saturated solution of a bisulphate of an alkali metal or ammonium, together with an excess of solid bisulphate for maintaining saturation may be employed for this purpose.
  • the electrolytic solution with which inert material is saturated, includes a surface active agent, comprising one or more non-polar long chain groups associated with a polar grouping consisting of one or more polar groups and resistant to deterioration by the electrolyte forming the remainder of the electrolytic solution. It has been found that the addition of such surface active agent inhibits adhesion of the lead sulphate layer to the lead anode, so that if space is available within the cell, the lead sulphate falls off the lead anode and the internal resistance remains low.
  • the surface active agent prevents the sulphate from forming into a continuous layer; therefore, conductivity is maintained at a satisfactory level through contact of the electrolyte with the portions of the anode not effectively covered by the sulphate.
  • the anode is preferably amalgamated, the purpose of amalgamation being to aid in inhibiting the adhesion of an electrically resistive lead sulphate layer to the anode, and to minimize the susceptibility of the anode to attack by the electrolyte when the cell is not being discharged.
  • the use of the surface active agent in the electrolytic solution permits the utilization of a solid lead anode instead of requiring a spongy lead type of anode such as that used in the conventional lead storage cell. As a result, the deterioration of the anode is less rapid and the life of the battery is increased in comparison With lead storage cells of conventional construction.
  • case 2 In order to prevent the formation of a thin layer of lead sulphate on the inner surface of conductive case 2, which constitutes the cathode of the cell, that case may have the inner surface anodized with a layer of lead dioxide. Any appropriate anodizing process may be used.
  • the case may be made the anode is an electrolytic process in which the electrolyte is lead nitrate; of course, caution must be exercised in maintaining the current density and the electrolyte concentration at appropriate values.
  • the sulphuric acid is dissipated by the formation of lead sulphate.
  • a cation exchange material such as sulfonated coal, it may be possible to bring about a partial regeneration of the sulphuric acid.
  • the use of such a cation exchange material provides hydrogen ions to displace the lead ions in solution.
  • case 2 may be of stainless steel or other conductive material not attacked by usual concentrations of sulphuric acid.
  • the cathode mixture may comprise a mixture of lead dioxide with finely divided carbon particles such as acetylene black or graphite.
  • the primary cell 8 includes an anode 9 of lead formed into a case, an inner container ID of chemically inert porous material such as a ceramic, a cathode conductor ll of lead or carbon supported within the inner container I0 and having cathode active material l2 of lead dioxide, or a mixture of lead dioxide with finely divided carbon particles, packed tightly in contact therewith and moistened with electrolytic solution.
  • Inner container H] is surrounded by inert material 13 Which is absorbent and which retains the electrolytic solution of the cell. Purely by way of example, spun glass may be employed for this purpose.
  • the electrolytic solution preferably contains a comparatively concentrated solution of sulphuric acid in addition to a surface active agent which is resistant to deterioration by the acid, such as an agent having one or more non-polar long chain groups associated with a polar grouping consisting of one or more polar groups.
  • a surface active agent which is resistant to deterioration by the acid, such as an agent having one or more non-polar long chain groups associated with a polar grouping consisting of one or more polar groups.
  • the anode 9 may be amalgamated as before.
  • the surface active agent in the electrolytic solution inhibits the formation of a continuous highly resistive layer of lead sulphate on the anode 9.
  • the cathode II is preferably anodized to prevent fcrmation of a film of lead sulphate on its surface.
  • the anode 9 of Figure 2 may be placed within a plastic cover [4 to prevent leakage through the case.
  • the cell 8 may be hermetically sealed by means of a heat fusible cap l5 constructed of tar, pitch, or the like.
  • a primary cell comprising: a lead anode; a cathode supported in spaced relation to said anode; a body of depolarizing material adjacent said cathode and spaced from said anode and comprising predominantly lead dioxide; and an electrolytic solution dispersed between said de- 5 polarizing body and said anode and including a sulphuric acid electrolyte and a surface active agent resistant to deterioration by said electrolyte, said surface active agent having a chemical composition comprising at least one non-polar long chain group associated with a polar grouping consisting of at least one polar group.

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Cell Separators (AREA)

Description

s. GLASSTONE PRIMARY CELLS Nov. 25, 1952 Filed May 21, 1948 Fig./
Fig.2
SAMUEL GLASSTONE I NVENTOR. JW
Patented Nov. 2 1952 PRIMARY CELLS Samuel Glasstone, Boston, Mass, assignor to Zenith Radio. Corporation, a corporation of Illinois ApplicationMay 21, 1948, Serial No. 28,468
1 Claim. 1
This invention relates to electrolytic apparatus, such as primary cells, apparatusincluding electrolytic baths and the like; It is a primary-object of the present invention to provide improved, apparatus of this type.
Presently known electrolytic methods for continually generating insoluble lead salts from a lead anode rely, in general, upon the presence in the electrolyte of critical concentrations of ions capable of forming soluble lead salts, and upon the maintenance of closely controlled current density. It is an important object of the present invention to provide improved electrolytic apparatus in which the current density and ion concentration are not limited by such necessity for critical control.
Presently available primary cells of the Leclanch type, incorporating zinc and carbon electrodes and an ammonium chloride electrolyte, suffer from several limitations. These limitations arise from the fact that polarization occurs at both carbon and zinc electrodes, such polarization resulting in decreased cell potential during operation. Furthermore, the watt hour capacity of such a cell is reduced when an increased rate of discharge is required. As an approximate numerical example, if a Leclanch cell is capable of delivering one watt hour of electricity when discharged at the rate of 5 milliamperes, it will yield in the order of only one-fifth of a Watt hour if the rate of discharge is increased to 50 milliamperes. The voltage obtainable from such a cell is too low for some applications; of even more importance, the volume efiiciency oi suchv a cell is seriously limited when the theoretically possible maximum volume efficiency is borne in mind.
Therefore it is an object of the invention to provide an improved primary cell.
It is a further important object of this invention to provide a primary cell in which the cell potential is substantially independent of current drain.
Yet a further object of the invention is to provide an improved primary cell of this type which is characterized by a substantially higher terminal voltage than that of' a conventional Leclanch cell.
Still a further object of the invention is to provide an improved primary cell which is capable of supplying large current output without I believed to be novel are set forth with particularity in the appended claim. The invention, to gether with further objects and advantages thereof, may more readily be understood, however, by reference to the following description taken in connection with the accompanying drawing, in which: V
Figure 1 is across sectionalview ofone embodiment of the present invention, and
Figure 2 is a cross sectional view of an alternative form of the embodiment shown in Figure 1-.
Throughout the specification and claim, that electrode at which metal tends to pass into solution as ions is referred to as the anode; the other electrode is referred to as the cathode. The polarity of the electrodes is conventionally referred to in connection wit-h the direction of current flow in the external circuit, the direction of current flow in the external circuit being from positive to negative. Ina primary cell, therefore, the anode as defined above is referred to as the negative electrode, andthe cathode as the positive electrode.
There is shown in Figure 1 as a preferred embodiment a primary cell l which includes a positive electrode or cathode comprising a case 2 of conductive material, such as lead; alternatively, case 2 may comprise lead or carbon deposited on the inner surface of a non-conductive material such as a plastic. Packed in close contact with the conductive inner surface of case 2 is a mixture or paste-3 of lead dioxide and electrolytic solution, an inner container 4 of porous chemically inert materialmay be provided to permit diffusion of electrolyte throughout the cell and to separate the mixture 3 from the inner electrode. As an example, the inner container 4 may be made of porous earthenware or woven glass. Chemically inert material 5, having large absorption capacity, may be packed into container 4 so as to provide means for retaining relatively large quantities of the electrolytic solution; such material may be, for example, glass Wool.
The negative electrode or anode 6 is of lead, preferably amalgamated and supported in the inert material 5 so as to be in contact with the electrolytic solution. The cell I may be hermetically sealed by a layer 1 of wax or pitch, which layer may also aid insupporting the negative electrodefi.
The. electrolytic solution includes sulphuric acid, and, in accordance with the present invention, a surface active agent composed of one or more-non-polarlong chain groups associated with a polar grouping consisting of one or more polar groups and substantially resistant to deterioration by sulphuric acid. -In one preferred embodiment, the surface active agent may be dodcylbenzene sodium sulfonate.
Other surface active agents which may be used are, for example, isopropyl naphthalene sodium sulfonate, sodium lauryl sulfate, sodium myristyl sulfate, and the alkyl phenoxypolyethoxyethanols, such as methyl phenoxypolyethoxyethanol.
In operation, when the external electrical circuit is conductively closed between negative terminal is connected to the anode 6 and positive terminal I! connected to the conductive case 2, current flows and the lead dioxide 3 is gradually reduced. A layer of lead sulphate tends to form upon the anode 6 until such time as all of the sulphate ions are combined with the lead anode, or until the anode is distintegrated. The acid used in the electrolytic solution should be of approximately 50% concentration, this being considerably higher than that used normally in lead storage cells. The reason for using such a high concentration of acid is to increase the volume efiiciency of the cell.
Furthermore the volume efficiency of the cell may be increased by the use of a saturated solution of a sulphate of an alkali metal or ammonium in the sulphuric acid electrolyte, together with an excess of solid sulphate to maintain saturation during cell discharge. As a further alternative, a saturated solution of a bisulphate of an alkali metal or ammonium, together with an excess of solid bisulphate for maintaining saturation, may be employed for this purpose.
As the cell discharges and a lead sulphate layer tends to form on the surface of the lead anode E, the internal resistance of the cell tends to increase. To prevent the resistance of the battery from increasing substantially, the electrolytic solution, with which inert material is saturated, includes a surface active agent, comprising one or more non-polar long chain groups associated with a polar grouping consisting of one or more polar groups and resistant to deterioration by the electrolyte forming the remainder of the electrolytic solution. It has been found that the addition of such surface active agent inhibits adhesion of the lead sulphate layer to the lead anode, so that if space is available within the cell, the lead sulphate falls off the lead anode and the internal resistance remains low. In the case of a cell construction like that of an ordinary flashlight dry cell where all the space within the cell is packed with functional material, the surface active agent prevents the sulphate from forming into a continuous layer; therefore, conductivity is maintained at a satisfactory level through contact of the electrolyte with the portions of the anode not effectively covered by the sulphate.
As has been previously mentioned, the anode is preferably amalgamated, the purpose of amalgamation being to aid in inhibiting the adhesion of an electrically resistive lead sulphate layer to the anode, and to minimize the susceptibility of the anode to attack by the electrolyte when the cell is not being discharged.
The use of the surface active agent in the electrolytic solution permits the utilization of a solid lead anode instead of requiring a spongy lead type of anode such as that used in the conventional lead storage cell. As a result, the deterioration of the anode is less rapid and the life of the battery is increased in comparison With lead storage cells of conventional construction.
In order to prevent the formation of a thin layer of lead sulphate on the inner surface of conductive case 2, which constitutes the cathode of the cell, that case may have the inner surface anodized with a layer of lead dioxide. Any appropriate anodizing process may be used. As an example, the case may be made the anode is an electrolytic process in which the electrolyte is lead nitrate; of course, caution must be exercised in maintaining the current density and the electrolyte concentration at appropriate values.
As the cell is discharged, the sulphuric acid is dissipated by the formation of lead sulphate. By the use of a cation exchange material such as sulfonated coal, it may be possible to bring about a partial regeneration of the sulphuric acid. The use of such a cation exchange material provides hydrogen ions to displace the lead ions in solution.
It is to be understood that the inner surface of case 2 may be of stainless steel or other conductive material not attacked by usual concentrations of sulphuric acid. Furthermore, the cathode mixture may comprise a mixture of lead dioxide with finely divided carbon particles such as acetylene black or graphite.
In Figure 2, the order of the cell elements is reversed from that shown in Figure 1. The primary cell 8 includes an anode 9 of lead formed into a case, an inner container ID of chemically inert porous material such as a ceramic, a cathode conductor ll of lead or carbon supported within the inner container I0 and having cathode active material l2 of lead dioxide, or a mixture of lead dioxide with finely divided carbon particles, packed tightly in contact therewith and moistened with electrolytic solution. Inner container H] is surrounded by inert material 13 Which is absorbent and which retains the electrolytic solution of the cell. Purely by way of example, spun glass may be employed for this purpose.
The electrolytic solution preferably contains a comparatively concentrated solution of sulphuric acid in addition to a surface active agent which is resistant to deterioration by the acid, such as an agent having one or more non-polar long chain groups associated with a polar grouping consisting of one or more polar groups. The anode 9 may be amalgamated as before. As in the case of the cell described in connection with Figure l, the surface active agent in the electrolytic solution inhibits the formation of a continuous highly resistive layer of lead sulphate on the anode 9.
The cathode II is preferably anodized to prevent fcrmation of a film of lead sulphate on its surface.
The anode 9 of Figure 2 may be placed within a plastic cover [4 to prevent leakage through the case. The cell 8 may be hermetically sealed by means of a heat fusible cap l5 constructed of tar, pitch, or the like.
While the invention has been shown and described in connection with a present preferred embodiment, it is apparent that numerous variations and modifications may be made, and it is therefore contemplated in the appended claim to cover all such variations and modifications as fall within the true spirit and scope of the invention.
I claim:
A primary cell comprising: a lead anode; a cathode supported in spaced relation to said anode; a body of depolarizing material adjacent said cathode and spaced from said anode and comprising predominantly lead dioxide; and an electrolytic solution dispersed between said de- 5 polarizing body and said anode and including a sulphuric acid electrolyte and a surface active agent resistant to deterioration by said electrolyte, said surface active agent having a chemical composition comprising at least one non-polar long chain group associated with a polar grouping consisting of at least one polar group.
SAMUEL GLASSTONE.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Name Date Swan Dec. 18, 1847 Number Number 10 Number
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2786088A (en) * 1952-09-09 1957-03-19 Sprague Electric Co Electrochemical systems
US2900434A (en) * 1956-01-03 1959-08-18 Union Carbide Corp Corrosion inhibitors
US2954418A (en) * 1958-04-22 1960-09-27 Ruben Samuel Lead peroxide dry cell
EP0871984A4 (en) * 1995-05-17 1998-10-21
US5976730A (en) * 1994-05-19 1999-11-02 White Eagle International Technologies, Inc. Electrical energy generation
US6225001B1 (en) * 1996-05-13 2001-05-01 White Eagle International Technologies, Inc. Electrical energy generation

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5400A (en) * 1847-12-18 Improvement in galvanic batteries for telegraphs
US1032623A (en) * 1911-12-26 1912-07-16 Charles J Reed Electrolytic process.
US1684852A (en) * 1928-06-05 1928-09-18 American Automotive Corp Electrolyte for storage batteries
US1901364A (en) * 1930-11-28 1933-03-14 Cummings Edmund Olin Process of making basic metal sulphates and recovery of metal from waste metallic compounds
GB389738A (en) * 1932-07-23 1933-03-23 Nl Electrolyt Mij Lightning Mi Improvements in or relating to electric accumulators
GB432775A (en) * 1934-10-26 1935-08-01 Leonard Fuller Improvements in or relating to electric storage cells or batteries
GB534618A (en) * 1938-08-04 1941-03-12 Hans Rudolph Improvements in or relating to porous diaphragms for electrolytic cells
US2275054A (en) * 1939-07-18 1942-03-03 Int Smelting & Refining Co Electrolytic production of lead sulpho-chromates
US2391289A (en) * 1941-09-15 1945-12-18 Jr John F Beaver Bright copper plating
US2441896A (en) * 1945-01-17 1948-05-18 Burgess Battery Co Emulsified battery electrolyte
US2490598A (en) * 1943-09-24 1949-12-06 Leonard Fuller Tubular secondary electric battery

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5400A (en) * 1847-12-18 Improvement in galvanic batteries for telegraphs
US1032623A (en) * 1911-12-26 1912-07-16 Charles J Reed Electrolytic process.
US1684852A (en) * 1928-06-05 1928-09-18 American Automotive Corp Electrolyte for storage batteries
US1901364A (en) * 1930-11-28 1933-03-14 Cummings Edmund Olin Process of making basic metal sulphates and recovery of metal from waste metallic compounds
GB389738A (en) * 1932-07-23 1933-03-23 Nl Electrolyt Mij Lightning Mi Improvements in or relating to electric accumulators
GB432775A (en) * 1934-10-26 1935-08-01 Leonard Fuller Improvements in or relating to electric storage cells or batteries
GB534618A (en) * 1938-08-04 1941-03-12 Hans Rudolph Improvements in or relating to porous diaphragms for electrolytic cells
US2275054A (en) * 1939-07-18 1942-03-03 Int Smelting & Refining Co Electrolytic production of lead sulpho-chromates
US2391289A (en) * 1941-09-15 1945-12-18 Jr John F Beaver Bright copper plating
US2490598A (en) * 1943-09-24 1949-12-06 Leonard Fuller Tubular secondary electric battery
US2441896A (en) * 1945-01-17 1948-05-18 Burgess Battery Co Emulsified battery electrolyte

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2786088A (en) * 1952-09-09 1957-03-19 Sprague Electric Co Electrochemical systems
US2900434A (en) * 1956-01-03 1959-08-18 Union Carbide Corp Corrosion inhibitors
US2954418A (en) * 1958-04-22 1960-09-27 Ruben Samuel Lead peroxide dry cell
US5976730A (en) * 1994-05-19 1999-11-02 White Eagle International Technologies, Inc. Electrical energy generation
WO2001033652A1 (en) * 1994-05-19 2001-05-10 Renaltech International Llc Electrical energy generation
EP0871984A4 (en) * 1995-05-17 1998-10-21
US6225001B1 (en) * 1996-05-13 2001-05-01 White Eagle International Technologies, Inc. Electrical energy generation

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