WO2009051925A1 - Battery electrode - Google Patents

Battery electrode Download PDF

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Publication number
WO2009051925A1
WO2009051925A1 PCT/US2008/076100 US2008076100W WO2009051925A1 WO 2009051925 A1 WO2009051925 A1 WO 2009051925A1 US 2008076100 W US2008076100 W US 2008076100W WO 2009051925 A1 WO2009051925 A1 WO 2009051925A1
Authority
WO
WIPO (PCT)
Prior art keywords
fabric
electrode
article
battery
carbonized
Prior art date
Application number
PCT/US2008/076100
Other languages
French (fr)
Inventor
Douglas J. Miller
Gary Dale Shives
Terence A. Pirro
Original Assignee
Graftech International Holdings Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Graftech International Holdings Inc. filed Critical Graftech International Holdings Inc.
Priority to JP2010600042U priority Critical patent/JP3165478U/en
Priority to CN2008901001616U priority patent/CN201873528U/en
Priority to US12/678,269 priority patent/US20100291440A1/en
Publication of WO2009051925A1 publication Critical patent/WO2009051925A1/en

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • H01M4/16Processes of manufacture
    • H01M4/20Processes of manufacture of pasted electrodes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/665Composites
    • H01M4/667Composites in the form of layers, e.g. coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/68Selection of materials for use in lead-acid accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/80Porous plates, e.g. sintered carriers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/56Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of lead
    • 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

  • Batteries especially lead acid batteries, each include at least one electrode, and generally at least one positive electrode and one negative electrode, as well as an electrolyte solution.
  • the reaction which permits the battery to store and release electrical energy occurs in a paste which is coated on and in the electrodes, with the role of the electrodes being to transfer current to and from the terminals of the battery.
  • two characteristics of the material used for forming the electrodes of a lead acid battery is its ability to retain thereon or therein a sufficient amount of paste for the desired level of functioning, and the ability of the material to withstand the corrosive environment within the battery, due in large part to the sulfuric acid commonly used in the electrolyte.
  • a material useful for forming, inter alia, an electrode in a lead acid battery which is not subject to extensive corrosion in an acidic environment over the expected lifetime of the lead acid battery is provided.
  • a material useful for forming, inter alia, an electrode in a battery and which has sufficient rigidity to provide the structure needed is provided.
  • Still another embodiment of the present invention provides a process for forming a material useful for forming an electrode in a battery which is sufficiently dimensionally stable for functioning as an electrode material, has large scale porosity for maintaining a sufficient amount of paste on or in the electrode, and is sufficiently corrosion resistant.
  • a material suitable for use as an electrode for a battery comprising an article which comprises carbonized cellulosic fabric, such as cotton (like cheesecloth), rayon or lyocell, having an impregnant therein, such as a resin or pitch; preferably, the article comprises a plurality (i.e., about 2 to about 10) of layers of carbonized fabric having an impregnant therein.
  • the article should be porous, and at least some of the pores at least partially filled with paste.
  • the inventive article is produced by the process involving providing a starting article comprising at least one layer of a fabric; carbonizing the starting article to form a carbonized fabric; impregnating the carbonized fabric with a material selected from the group consisting of resin, pitch, or combinations thereof to form an impregnated article; curing the impregnated article in the case of impregnated articles to form a cured article; and carbonizing the cured article.
  • the inventive process involves providing a starting article comprising at least one layer of a fabric; partially carbonizing the starting article to form a partially carbonized fabric; impregnating the partially carbonized fabric with a material selected from the group consisting of resin, pitch, or combinations thereof to form an impregnated article; curing the impregnated article in the case of impregnated articles to form a cured article; and completing carbonization of the cured article.
  • cure and completion of carbonization can be accomplished in one step.
  • the fabric can be treated with a halide and/or a depolymerization inhibitor prior to carbonization.
  • the impregnation/cure steps can be repeated at least two times.
  • Fig. 1 is a partially broken-away side perspective view of a lead acid battery containing an electrode in accordance with the present invention.
  • Fig. 2 is a plan view of an electrode in accordance with the present invention.
  • Fig. 3 is a cross-sectional view of the electrode of Fig. 2, taken along lines 3-3 of Fig. 2.
  • Fig. 4 is a partial plan view of the electrode of Fig. 2.
  • an energy storage device such as a battery is denoted with the reference numeral 10.
  • battery 10 may be a lead acid battery.
  • Other examples of an energy storage device may include a capacitor or a super capacitor.
  • Battery 10 generally comprises a case or housing 12 within which an electrolyte solution is maintained.
  • the electrolyte solution consists of a mixture of sulfuric acid and water (especially distilled water), although other additives along with or in place of sulfuric acid and water can be employed.
  • Also positioned within battery 10 is at least one cell 20, electrically connected with at least one battery terminal 14 positioned on an outer portion of case 12.
  • battery 10 comprises a plurality of cells 20a, 20b, etc., connected in series or in parallel, depending on the desired capacity of battery 10.
  • Each cell 20a, 20b, etc. of battery 10 comprises a plurality of electrodes 30, alternating between positive electrodes 32 and negative electrodes 34, which are immersed in the electrolyte solution.
  • Positive electrodes 32 are filled with a chemically active paste, such as lead dioxide (Pb ⁇ 2) or other conventional materials, which serves as the active material of positive electrodes 32.
  • Negative plates 34 may contain a lead dioxide paste as active material, or a different material such as a sponge lead material or other suitable material as the active material of negative plates 34.
  • Sponge lead is a form of metallic lead brought to a spongy form by reduction of lead salts, or by compressing finely divided lead.
  • the potential difference that exists between the active material of positive electrode 32 and the active material of negative electrode 34 when immersed in the electrolytic solution causes electrons to flow from negative electrode 34 to positive electrode 32, and which reduces the lead dioxide at positive electrode 32 to form lead sulfate (PbSO 4 ); at negative electrode 34, sponge lead is oxidized to form lead sulfate.
  • a counter- voltage may be applied to the battery terminals to force a current through the cells in a direction opposite to that in which the cell discharges.
  • the cell reactions of the discharge process may be reversed. Specifically, the lead sulfate at positive electrode 32 is converted back to lead dioxide, and the lead sulfate at negative electrode 34 is converted back to sponge lead.
  • the material from which electrode 30 is formed must be capable of being filled with sufficient active material (i.e., lead dioxide paste or sponge lead) to provide battery 10 of which electrode 30 is an element with sufficient capacity.
  • the material from which electrode 30 is formed may have large scale porosity, by which is meant sufficiently large pores to permit the pores of the material to be at least partially filled with a paste of the viscosity of lead dioxide or sponge lead pastes. It will be recognized by the skilled artisan that not all of the pores of an electrode 30 are filled with the active material paste, and that even those pores which have paste therein may not be 100% filled (volumetrically) with paste.
  • the pore structure should retain a majority of the paste, preferably about all of the paste, more preferably all of the paste, and provide efficient contacting of the paste with both the electrolyte and the electrode.
  • the material from which electrodes 30 are formed should also be relatively resistant to corrosion, especially in the acidic environment of the electrolyte in a battery, especially a lead acid battery. More particularly, the material should be less corrosive (i.e., have a slower rate of corrosion) than conventional materials used to form battery electrodes, such as lead or alloys of lead with, for instance, antimony, cadmium, tin, or any other suitable elements.
  • the corrosion rate can depend on, inter alia, ambient temperature, battery operating temperature, electrode potential, acid concentration in the electrolyte, etc., as well as the corrosion resistance offered by electrode 30. Corrosion may occur over a large area of each electrode 30, or it may occur at localized areas.
  • electrodes 30 will vary with the particular battery application. In other words, for certain battery applications, greater porosity may be more beneficial than others; likewise, for certain battery applications, greater corrosion resistance will be more beneficial than others.
  • the pore structure of the inventive material may be designed so as to provide an efficient use of paste, and the electrode material may be able to provide varying degrees of electrical and thermal conductivity for the particular requirements of particular embodiments of a battery. Accordingly, the process used to produce the inventive material should provide the flexibility to produce materials having differing characteristics depending on the particular battery or other application for which it is intended.
  • electrode 30 is employed as positive electrode 32.
  • electrode 30 may be used as cathode of a super capacitor.
  • a material suitable for use as electrode 30 can be formed of a carbonized fabric, by which is meant a cloth made by weaving, knitting, stitching or felting fibers, and which is thereafter carbonized, especially by heat.
  • Suitable fabrics can include those which can be carbonized in high yield such as cellulose based textiles i.e. cotton, rayon, lyocell fabrics, or combinations thereof, and can be used singly or in layers.
  • the design of the fabric as well as the scheme for layering contributes to the ultimate size and shape of the pores in the final electrode. In one embodiment, from 2 to about 19 layers of fabric have been found to be especially useful for the production of a material which can function as electrode 30 for battery 10.
  • the choice of the fabric employed can be used to "engineer" the characteristics of the material used for electrode 30.
  • the pore size and distribution of the starting fabric can determine the pore size and distribution of the finished material, and thus, the finished material can be tailored to the needs of the specific battery application for which it is intended.
  • a combination of fabrics having differing characteristics can be layered together to provide a unique carbonized material for use as electrode 30.
  • the first step in the process is to select or design and produce a fabric structure that has the desired thread diameter and size and shape of openings in the fabric to produce a material having the desired structure for electrode 30.
  • a preferred structure is a cotton cheesecloth of 10 x 25 threads per inch ("TPI"); a second embodiment is about al2 x 20 TPI cheesecloth; and a third embodiment is about 15 x 15 TPI cheesecloth.
  • Preferred thread diameters range from about 150 to 400 microns, preferably at least 200 micron, more preferably about 250 microns.
  • At least one layer of a fabric is carbonized.
  • the individual layers can be carbonized separately, before being laid up into the multi-layer material, or the fabric layers can be laid up prior to carbonization.
  • carbonization of the fabric layer(s) occurs at a temperature between about 300°C to about 1000°C, more preferably about 650°C to about 800°C, in an inert or oxygen-free atmosphere, such as a nitrogen atmosphere.
  • carbonization temperatures are generally reached by raising the temperature in a slow and controlled manner, such as from about 5°C to about 50°C per hour, preferably up to 30°C per hour, and the fabric is maintained at the carbonization temperature for a period of at least about several minutes to up to about 3 hours, preferably about 30 minutes up to about 2 hours, more preferably at least about 1 hour.
  • the fabric is first impregnated with a halide to increase the carbon yield after carbonization, as discussed in U.S. Patent No. 3,479,151, the disclosure of which is incorporated herein by reference. More specifically, carbonization occurs after impregnating the layers (either before or after being laid up) with a neutral or slightly acidic hygroscopic halide. In this case the carbonization process may be accelerated so that the total process time can be reduced to less than 1 hour. This makes practical a continuous carbonization furnace in which the fabric is fed from a roll at the inlet and the carbonized cloth is collected on a roll at the outlet.
  • the halide employed is preferably a neutral or slightly acidic salt, and may comprise, for example, calcium chloride, magnesium chloride, ammonium chloride, etc., or a halide of a metal such as aluminum or higher atomic weight metal such as titanium, manganese, zirconium, or thorium.
  • a depolymerization inhibitor may be employed during carbonization, together with the halide, to prevent loss of carbon from the structure, as by depolymerization and dissipation as carbon oxides, etc.
  • the depolymerization inhibitor suitably comprises ammonia, an alkyl amine or an ammonium halide, or alkyl ammonium halide. It will be noted that the depolymerization inhibitor can also be the halide salt.
  • the neutral or slightly acidic halide salt (which optionally may incorporate the depolymerization inhibitor) may be impregnated into the fabric prior to carbonization. Impregnation is accomplished, for instance, by contacting the fabric in any suitable manner, as by spraying, etc., with the selected impregnant in a sufficient concentration.
  • the selected halide salt is soluble or at least readily dispersible in water and, accordingly, is used in an aqueous solution or dispersion into which the fabric is immersed.
  • alcohol or other suitable solvents or dispersants compatible with the fabric can also be used.
  • a concentration of 0.1 mol or more of the halide salt is characteristically employed, usually about 0.5 mol or more.
  • the impregnation of the fabric with the halide can be carried out for at least about 1 minute for sufficient effect, while times greater than about 5 minutes are generally not necessary.
  • drying of the impregnated fabric prior to carbonization can be carried out, for example by exposing the impregnated fabric to a temperature below carbonizing temperature.
  • impregnated cloth with calcium chloride in aqueous solution can be dried by heating the drained cloth in air to about 120 2 C and holding it at that temperature for, for example, about 15 minutes.
  • Carbonization of the impregnated fabric can then be initiated by increasing the temperature of the impregnated fabric, as described above.
  • the carbonized fabric is laid up into the desired number of layers in a support frame (if not laid up prior to carbonization) and impregnated with a resin or a pitch.
  • the particular resin or pitch impregnant employed can vary depending on the particular characteristics desired for electrodes 30, as well as the operating environment of battery 10 (such as conditions like operating temperature, nature of the electrolyte, etc.).
  • Resins found especially useful in the practice of the present invention include acrylic-, epoxy- and phenolic-based resin systems, fluoro-based polymers, or mixtures thereof.
  • Suitable epoxy resin systems include those based on diglycidyl ether of bisphenol A (DGEBA) and other multifunctional resin systems; a non-limiting example of phenolic resins that can be employed include resole and novolac phenolics. Especially preferred is a furfuryl or polyfurfuryl resin system, employed with a catalyst such as maleic anhydride.
  • Suitable resin or pitch content in the carbonized fabric is preferably enough to fill from about 50% to about 100% of available void space in the thread or yarn that makes up the fabric.
  • the impregnant is cured (although it will be recognized that the term cure is more applicable to resin impregnation, rather than pitch impregnation, the skilled artisan will understand what is meant by cure of a pitch impregnant; specifically, removal of the volatiles in the pitch), such as by bringing the impregnant to a temperature above the cure temperature of the particular impregnant system employed. For polyfurfuryl resin systems, curing at a temperature of at least about 130 2 C should be sufficient, although the specific cure conditions would be within the skill of the artisan.
  • impregnant While one application of impregnant is often sufficient, depending on the particular characteristics for electrode 30 that are desired, such as dimensional stability and rigidity, several cycles of resin impregnation/cure as described above may be effected.
  • the resin pickup may be tightly controlled. Such pickup may be controlled down to the level of individual layers.
  • An air knife may be used to control the resin pick up by removing excess resin from the carbonized material. The number of passes under the air knife, the operation pressure of the knife, and the exposure time of the knife to the carbonized cloth may all be varied to control density.
  • Another technique that may be used to control density is the use of a mask during the initial stages of the curing of the resin. This technique may be used to achieve a low density product.
  • the spacing of the layers of the material apart and shrinkage of the material during curing and/or carbonization may be used to control density.
  • impregnation treatments build on the surface of the threads that makeup the fabric.
  • the fabric is drained well or subjected to a flow of gas so as to keep impregnant from bridging the openings in the fabric that will ultimately become the pores of the carbon structure.
  • at least 3 and up to 10 impregnation/cure cycles may be advantageously employed. In some instances more than 10 resin impregnation/cure cycles may be employed.
  • impregnation with a resin is preferred, impregnation with a material other than a resin may be desirable, depending on the material characteristics desired. For instance, impregnation with a pitch may provide benefits, especially in terms of conductivity of the finished material.
  • the resin impregnated fabric(s) is then subject to another carbonization step.
  • carbonization occurs at a temperature between about 300°C to about 1000°C, more preferably about 650°C to about 800°C, advantageously in an inert or oxygen-free atmosphere, such as a nitrogen atmosphere.
  • Carbonization temperatures are generally reached by raising the temperature in a slow and controlled manner, such as from about 5°C to about 50°C per hour, and the material is maintained at the carbonization temperature for a period of at least about 30 minutes to about 2 hours, more preferably for about 1 hour.
  • the fabric may be restrained, or otherwise held in position, in order to avoid warping and to ensure that the finished material has the proper shape, flatness or other special characteristics.
  • the resulting carbon or graphite article has the porous structure suitable for filling the pores with a paste, as is beneficial for use as electrodes 30 in battery 10.
  • the presence of the paste within the porous structure permits the electrolyte to permeate through the body of electrode 30, and not just react at the face of the electrode; thus, the whole body of electrode 30 is a reaction site, not just the face.
  • the dimensional stability of the carbonized fabric and corrosion resistance makes it uniquely suitable for use as an electrode in a battery, especially a lead acid battery.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Composite Materials (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Cell Electrode Carriers And Collectors (AREA)

Abstract

A material suitable for use as an electrode for a battery, comprising an article which comprises carbonized fabric having an impregnant therein.

Description

BATTERY ELECTRODE BACKGROUND OF THE INVENTION
TECHNICAL FIELD [0001] Batteries, especially lead acid batteries, each include at least one electrode, and generally at least one positive electrode and one negative electrode, as well as an electrolyte solution. The reaction which permits the battery to store and release electrical energy occurs in a paste which is coated on and in the electrodes, with the role of the electrodes being to transfer current to and from the terminals of the battery. Thus, two characteristics of the material used for forming the electrodes of a lead acid battery is its ability to retain thereon or therein a sufficient amount of paste for the desired level of functioning, and the ability of the material to withstand the corrosive environment within the battery, due in large part to the sulfuric acid commonly used in the electrolyte.
[0002] In the past, there have been several proposed methods for inhibiting corrosion of battery electrodes, such as those formed of a lead grid. For instance, in G.Br. Patent No. 18,590, the electrodes are protected from corrosion by treating the electrode grids with a mixture of rubber, antimony, and graphite, by either dipping the grids into the mixture or by brushing the mixture onto the grids with a brush.
[0003] Contrariwise, in U.S. Patent No. 7,105,252, a method of forming a coated electrode for a battery is proposed, where the electrode is exposed to an environment including vaporized carbon such that at least some carbon from the environment may be transferred to the electrode. [0004] Unfortunately, prior attempts to provide an electrode material which is both capable of maintaining sufficient paste for proper functioning of the battery and which is sufficiently corrosion resistant have not been satisfactory. What is desired, then, is a material which is sufficiently dimensionally stable for functioning as an electrode material, has a high degree of porosity for maintaining a sufficient amount of paste on or in the electrode, and is sufficiently corrosion resistant. Moreover, a process for forming the desired material is also advantageous, especially when the process permits the formation of a wide variety of suitable materials, having differing porosities with highly controlled shape and size for different battery applications.
BRIEF DESCRIPTION
[0005] Accordingly, it is an embodiment of the present invention to provide a material useful for forming, inter alia, an electrode in a battery which is sufficiently dimensionally stable for functioning as an electrode material, has high porosity for maintaining a sufficient amount of paste on or in the electrode.
[0006] It is another embodiment of the present invention to provide a material useful for forming, inter alia, an electrode in a battery having sufficient porosity for maintaining a sufficient amount of paste on or in the electrode, wherein the structure of the porosity is designed to provide efficient contacting of the paste with both the electrolyte and the electrode and the electrode material is sufficiently corrosion resistant and electrically conductive.
[0007] In another embodiment of the present invention, a material useful for forming, inter alia, an electrode in a lead acid battery which is not subject to extensive corrosion in an acidic environment over the expected lifetime of the lead acid battery is provided. [0008] In is still another embodiment of the present invention a material useful for forming, inter alia, an electrode in a battery and which has sufficient rigidity to provide the structure needed is provided.
[0009] It is yet another embodiment of the present invention to provide a material useful for forming, inter alia, an electrode in a lead acid battery, which is sufficiently porous to permit paste to be incorporated thereinto.
[0010] Still another embodiment of the present invention provides a process for forming a material useful for forming an electrode in a battery which is sufficiently dimensionally stable for functioning as an electrode material, has large scale porosity for maintaining a sufficient amount of paste on or in the electrode, and is sufficiently corrosion resistant.
[0011] It is yet another embodiment of the present invention to provide a process for forming a material useful for forming an electrode in a lead acid battery, which can be used to produce materials having differing characteristics, as desired.
[0012] These embodiments and others which will be apparent to the skilled artisan upon reading the following description, can be achieved by providing a material suitable for use as an electrode for a battery, comprising an article which comprises carbonized cellulosic fabric, such as cotton (like cheesecloth), rayon or lyocell, having an impregnant therein, such as a resin or pitch; preferably, the article comprises a plurality (i.e., about 2 to about 10) of layers of carbonized fabric having an impregnant therein. For use as an electrode, the article should be porous, and at least some of the pores at least partially filled with paste. [0013] The inventive article is produced by the process involving providing a starting article comprising at least one layer of a fabric; carbonizing the starting article to form a carbonized fabric; impregnating the carbonized fabric with a material selected from the group consisting of resin, pitch, or combinations thereof to form an impregnated article; curing the impregnated article in the case of impregnated articles to form a cured article; and carbonizing the cured article. Alternatively, the inventive process involves providing a starting article comprising at least one layer of a fabric; partially carbonizing the starting article to form a partially carbonized fabric; impregnating the partially carbonized fabric with a material selected from the group consisting of resin, pitch, or combinations thereof to form an impregnated article; curing the impregnated article in the case of impregnated articles to form a cured article; and completing carbonization of the cured article. Indeed, cure and completion of carbonization can be accomplished in one step. The fabric can be treated with a halide and/or a depolymerization inhibitor prior to carbonization. Moreover, the impregnation/cure steps can be repeated at least two times.
[0014] It is to be understood that both the foregoing general description and the following detailed description present embodiments of the invention, and are intended to provide an overview or framework for understanding the nature and character of the invention as it is claimed. The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification. The drawings illustrate various embodiments of the invention and together with the description serve to explain the principles and operations of the invention. BRIEF DESCRIPTION OF THE DRAWINGS
[0015] Fig. 1 is a partially broken-away side perspective view of a lead acid battery containing an electrode in accordance with the present invention.
[0016] Fig. 2 is a plan view of an electrode in accordance with the present invention.
[0017] Fig. 3 is a cross-sectional view of the electrode of Fig. 2, taken along lines 3-3 of Fig. 2.
[0018] Fig. 4 is a partial plan view of the electrode of Fig. 2.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0019] Referring now to the Figures, and especially to Fig. 1, an energy storage device such as a battery is denoted with the reference numeral 10. One embodiment of battery 10 may be a lead acid battery. Other examples of an energy storage device may include a capacitor or a super capacitor. Battery 10 generally comprises a case or housing 12 within which an electrolyte solution is maintained. Conventionally, the electrolyte solution consists of a mixture of sulfuric acid and water (especially distilled water), although other additives along with or in place of sulfuric acid and water can be employed. Also positioned within battery 10 is at least one cell 20, electrically connected with at least one battery terminal 14 positioned on an outer portion of case 12.
Typically, battery 10 comprises a plurality of cells 20a, 20b, etc., connected in series or in parallel, depending on the desired capacity of battery 10.
[0020] Each cell 20a, 20b, etc. of battery 10 comprises a plurality of electrodes 30, alternating between positive electrodes 32 and negative electrodes 34, which are immersed in the electrolyte solution. Positive electrodes 32 are filled with a chemically active paste, such as lead dioxide (Pbθ2) or other conventional materials, which serves as the active material of positive electrodes 32. Negative plates 34 may contain a lead dioxide paste as active material, or a different material such as a sponge lead material or other suitable material as the active material of negative plates 34. Sponge lead is a form of metallic lead brought to a spongy form by reduction of lead salts, or by compressing finely divided lead.
[0021] In operation, the potential difference that exists between the active material of positive electrode 32 and the active material of negative electrode 34 when immersed in the electrolytic solution causes electrons to flow from negative electrode 34 to positive electrode 32, and which reduces the lead dioxide at positive electrode 32 to form lead sulfate (PbSO4); at negative electrode 34, sponge lead is oxidized to form lead sulfate. In a charging process, a counter- voltage may be applied to the battery terminals to force a current through the cells in a direction opposite to that in which the cell discharges. As a result, the cell reactions of the discharge process may be reversed. Specifically, the lead sulfate at positive electrode 32 is converted back to lead dioxide, and the lead sulfate at negative electrode 34 is converted back to sponge lead.
[0022] Accordingly, the material from which electrode 30 is formed must be capable of being filled with sufficient active material (i.e., lead dioxide paste or sponge lead) to provide battery 10 of which electrode 30 is an element with sufficient capacity. Accordingly, the material from which electrode 30 is formed may have large scale porosity, by which is meant sufficiently large pores to permit the pores of the material to be at least partially filled with a paste of the viscosity of lead dioxide or sponge lead pastes. It will be recognized by the skilled artisan that not all of the pores of an electrode 30 are filled with the active material paste, and that even those pores which have paste therein may not be 100% filled (volumetrically) with paste. Rather, when reference is made herein to filling the pores of a material with paste, what is being referred to is that a large enough fraction of the pores (typically at least about 30%, more typically at least about 40% and desirably between about 50% and about 100%) are sufficiently filled with paste (preferably at least about 25% on a volumetric basis, more preferably at least about 45% and most preferably between about 50% and about 100% on a volumetric basis) to permit effective use of the material as electrode 30 in battery 10. In one embodiment, the pore structure should retain a majority of the paste, preferably about all of the paste, more preferably all of the paste, and provide efficient contacting of the paste with both the electrolyte and the electrode.
[0023] In addition, the material from which electrodes 30 are formed should also be relatively resistant to corrosion, especially in the acidic environment of the electrolyte in a battery, especially a lead acid battery. More particularly, the material should be less corrosive (i.e., have a slower rate of corrosion) than conventional materials used to form battery electrodes, such as lead or alloys of lead with, for instance, antimony, cadmium, tin, or any other suitable elements. The corrosion rate can depend on, inter alia, ambient temperature, battery operating temperature, electrode potential, acid concentration in the electrolyte, etc., as well as the corrosion resistance offered by electrode 30. Corrosion may occur over a large area of each electrode 30, or it may occur at localized areas.
[0024] It will be recognized that the specific characteristics for the material used for the formation of electrodes 30 will vary with the particular battery application. In other words, for certain battery applications, greater porosity may be more beneficial than others; likewise, for certain battery applications, greater corrosion resistance will be more beneficial than others. Furthermore, the pore structure of the inventive material may be designed so as to provide an efficient use of paste, and the electrode material may be able to provide varying degrees of electrical and thermal conductivity for the particular requirements of particular embodiments of a battery. Accordingly, the process used to produce the inventive material should provide the flexibility to produce materials having differing characteristics depending on the particular battery or other application for which it is intended. In one particular embodiment, electrode 30 is employed as positive electrode 32. In addition to the above, in another particular embodiment, electrode 30 may be used as cathode of a super capacitor.
[0025] In accordance with the present invention, a material suitable for use as electrode 30 can be formed of a carbonized fabric, by which is meant a cloth made by weaving, knitting, stitching or felting fibers, and which is thereafter carbonized, especially by heat.
[0026] Suitable fabrics can include those which can be carbonized in high yield such as cellulose based textiles i.e. cotton, rayon, lyocell fabrics, or combinations thereof, and can be used singly or in layers. The design of the fabric as well as the scheme for layering contributes to the ultimate size and shape of the pores in the final electrode. In one embodiment, from 2 to about 19 layers of fabric have been found to be especially useful for the production of a material which can function as electrode 30 for battery 10. The choice of the fabric employed can be used to "engineer" the characteristics of the material used for electrode 30. In other words, the pore size and distribution of the starting fabric can determine the pore size and distribution of the finished material, and thus, the finished material can be tailored to the needs of the specific battery application for which it is intended. Indeed, a combination of fabrics having differing characteristics can be layered together to provide a unique carbonized material for use as electrode 30.
[0027] The first step in the process is to select or design and produce a fabric structure that has the desired thread diameter and size and shape of openings in the fabric to produce a material having the desired structure for electrode 30. One an embodiment of a preferred structure is a cotton cheesecloth of 10 x 25 threads per inch ("TPI"); a second embodiment is about al2 x 20 TPI cheesecloth; and a third embodiment is about 15 x 15 TPI cheesecloth. Preferred thread diameters range from about 150 to 400 microns, preferably at least 200 micron, more preferably about 250 microns.
[0028] The next step in the production of the material useful for electrode
30, at least one layer of a fabric is carbonized. When a plurality of layers are to be employed, the individual layers can be carbonized separately, before being laid up into the multi-layer material, or the fabric layers can be laid up prior to carbonization. In either case, carbonization of the fabric layer(s) occurs at a temperature between about 300°C to about 1000°C, more preferably about 650°C to about 800°C, in an inert or oxygen-free atmosphere, such as a nitrogen atmosphere. In one embodiment, carbonization temperatures are generally reached by raising the temperature in a slow and controlled manner, such as from about 5°C to about 50°C per hour, preferably up to 30°C per hour, and the fabric is maintained at the carbonization temperature for a period of at least about several minutes to up to about 3 hours, preferably about 30 minutes up to about 2 hours, more preferably at least about 1 hour.
[0029] In one embodiment, the fabric is first impregnated with a halide to increase the carbon yield after carbonization, as discussed in U.S. Patent No. 3,479,151, the disclosure of which is incorporated herein by reference. More specifically, carbonization occurs after impregnating the layers (either before or after being laid up) with a neutral or slightly acidic hygroscopic halide. In this case the carbonization process may be accelerated so that the total process time can be reduced to less than 1 hour. This makes practical a continuous carbonization furnace in which the fabric is fed from a roll at the inlet and the carbonized cloth is collected on a roll at the outlet.
[0030] The halide employed is preferably a neutral or slightly acidic salt, and may comprise, for example, calcium chloride, magnesium chloride, ammonium chloride, etc., or a halide of a metal such as aluminum or higher atomic weight metal such as titanium, manganese, zirconium, or thorium.
[0031] Advantageously, a depolymerization inhibitor may be employed during carbonization, together with the halide, to prevent loss of carbon from the structure, as by depolymerization and dissipation as carbon oxides, etc. The depolymerization inhibitor suitably comprises ammonia, an alkyl amine or an ammonium halide, or alkyl ammonium halide. It will be noted that the depolymerization inhibitor can also be the halide salt.
[0032] The neutral or slightly acidic halide salt (which optionally may incorporate the depolymerization inhibitor) may be impregnated into the fabric prior to carbonization. Impregnation is accomplished, for instance, by contacting the fabric in any suitable manner, as by spraying, etc., with the selected impregnant in a sufficient concentration. Usually, the selected halide salt is soluble or at least readily dispersible in water and, accordingly, is used in an aqueous solution or dispersion into which the fabric is immersed. Alternatively, alcohol or other suitable solvents or dispersants compatible with the fabric can also be used. A concentration of 0.1 mol or more of the halide salt is characteristically employed, usually about 0.5 mol or more. The impregnation of the fabric with the halide can be carried out for at least about 1 minute for sufficient effect, while times greater than about 5 minutes are generally not necessary.
[0033] If desired, drying of the impregnated fabric prior to carbonization can be carried out, for example by exposing the impregnated fabric to a temperature below carbonizing temperature. For example, impregnated cloth with calcium chloride in aqueous solution can be dried by heating the drained cloth in air to about 1202C and holding it at that temperature for, for example, about 15 minutes. Carbonization of the impregnated fabric can then be initiated by increasing the temperature of the impregnated fabric, as described above.
[0034] After carbonization (or, as noted above, at least partial carbonization), the carbonized fabric is laid up into the desired number of layers in a support frame (if not laid up prior to carbonization) and impregnated with a resin or a pitch. The particular resin or pitch impregnant employed can vary depending on the particular characteristics desired for electrodes 30, as well as the operating environment of battery 10 (such as conditions like operating temperature, nature of the electrolyte, etc.). Resins found especially useful in the practice of the present invention include acrylic-, epoxy- and phenolic-based resin systems, fluoro-based polymers, or mixtures thereof. Some examples of suitable epoxy resin systems include those based on diglycidyl ether of bisphenol A (DGEBA) and other multifunctional resin systems; a non-limiting example of phenolic resins that can be employed include resole and novolac phenolics. Especially preferred is a furfuryl or polyfurfuryl resin system, employed with a catalyst such as maleic anhydride. Suitable resin or pitch content in the carbonized fabric is preferably enough to fill from about 50% to about 100% of available void space in the thread or yarn that makes up the fabric. [0035] After impregnation, the impregnant is cured (although it will be recognized that the term cure is more applicable to resin impregnation, rather than pitch impregnation, the skilled artisan will understand what is meant by cure of a pitch impregnant; specifically, removal of the volatiles in the pitch), such as by bringing the impregnant to a temperature above the cure temperature of the particular impregnant system employed. For polyfurfuryl resin systems, curing at a temperature of at least about 1302C should be sufficient, although the specific cure conditions would be within the skill of the artisan. While one application of impregnant is often sufficient, depending on the particular characteristics for electrode 30 that are desired, such as dimensional stability and rigidity, several cycles of resin impregnation/cure as described above may be effected. If the density of the material to make electrode 30 is a concern, the resin pickup may be tightly controlled. Such pickup may be controlled down to the level of individual layers. An air knife may be used to control the resin pick up by removing excess resin from the carbonized material. The number of passes under the air knife, the operation pressure of the knife, and the exposure time of the knife to the carbonized cloth may all be varied to control density. Another technique that may be used to control density is the use of a mask during the initial stages of the curing of the resin. This technique may be used to achieve a low density product. Lastly the spacing of the layers of the material apart and shrinkage of the material during curing and/or carbonization may be used to control density.
Once the threads are saturated with cured resin, additional treatments build on the surface of the threads that makeup the fabric. After each impregnation treatment the fabric is drained well or subjected to a flow of gas so as to keep impregnant from bridging the openings in the fabric that will ultimately become the pores of the carbon structure. For instance, at least 3 and up to 10 impregnation/cure cycles may be advantageously employed. In some instances more than 10 resin impregnation/cure cycles may be employed. [0036] While impregnation with a resin is preferred, impregnation with a material other than a resin may be desirable, depending on the material characteristics desired. For instance, impregnation with a pitch may provide benefits, especially in terms of conductivity of the finished material.
[0037] After impregnation/cure, the resin impregnated fabric(s) is then subject to another carbonization step. As with the first, for this latter carbonization occurs at a temperature between about 300°C to about 1000°C, more preferably about 650°C to about 800°C, advantageously in an inert or oxygen-free atmosphere, such as a nitrogen atmosphere. Carbonization temperatures are generally reached by raising the temperature in a slow and controlled manner, such as from about 5°C to about 50°C per hour, and the material is maintained at the carbonization temperature for a period of at least about 30 minutes to about 2 hours, more preferably for about 1 hour.
Further heat treatment to graphitizing temperatures of greater than about 2000°C, and generally in the range of about 2000°C to about 3200°C may also be undertaken to lower electrical resistance.
[0038] In another embodiment, during processing the fabric may be restrained, or otherwise held in position, in order to avoid warping and to ensure that the finished material has the proper shape, flatness or other special characteristics.
[0039] The resulting carbon or graphite article has the porous structure suitable for filling the pores with a paste, as is beneficial for use as electrodes 30 in battery 10. The presence of the paste within the porous structure permits the electrolyte to permeate through the body of electrode 30, and not just react at the face of the electrode; thus, the whole body of electrode 30 is a reaction site, not just the face. Moreover, the dimensional stability of the carbonized fabric and corrosion resistance makes it uniquely suitable for use as an electrode in a battery, especially a lead acid battery.
[0040] The disclosures of all cited patents and publications referred to in this application are incorporated herein by reference.
[0041] The above description is intended to enable the person skilled in the art to practice the invention. It is not intended to detail all of the possible variations and modifications that will become apparent to the skilled worker upon reading the description. It is intended, however, that all such modifications and variations be included within the scope of the invention that is defined by the following claims. The claims are intended to cover the indicated elements and steps in any arrangement or sequence that is effective to meet the objectives intended for the invention, unless the context specifically indicates the contrary.

Claims

What is claimed is:
1. A material suitable for use as an electrode for an energy storage device, comprising an article which comprises carbonized fabric having an impregnant therein.
2. The material of claim 1, wherein the article comprises a plurality of layers of carbonized fabric having an impregnant therein.
3. The material of claim 2, wherein the article comprises from about 2 to about 10 layers of carbonized fabric having an impregnant therein.
4. The material of claim 1, wherein the fabric is comprised of cellulosic fibers such as cotton, rayon, lyocell or combinations thereof.
5. The material of claim 1, wherein the impregnant comprises a resin.
6. The material of claim 1, wherein the impregnant comprises pitch.
7. A lead acid battery, comprising an electrolyte and at least one electrode, wherein the electrode comprises a porous carbonized fabric, at least some of the pores of the carbonized fabric at least partially filled with a paste.
8. The battery of claim 7, wherein the electrode comprises a plurality of layers of carbonized fabric.
9. The battery of claim 7, wherein the fabric comprises cotton.
10. The battery of claim 7, wherein the fabric is graphitized.
11. A process for preparing a material suitable for use as an electrode for a lead acid battery, the process comprising:
(a) providing a starting article comprising at least one layer of a fabric;
(b) at least partially carbonizing the starting article to form a carbonized fabric; (c) impregnating the carbonized fabric with a material selected form the group consisting of resin, pitch, or combinations thereof to form an impregnated article;
(d) curing the impregnated article to form a cured article; and
(e) carbonizing the cured article.
12. The process of claim 14, wherein the starting article comprises a plurality of layers of fabric.
13. The process of claim 14, wherein the starting article is treated with a halide prior to carbonization.
14. The process of claim 14, wherein the starting article is treated with a depolymerization inhibitor prior to carbonization.
15. The process of claim 14, wherein steps (c) and (d) are repeated at least two times.
PCT/US2008/076100 2007-10-16 2008-09-12 Battery electrode WO2009051925A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012055731A1 (en) * 2010-10-25 2012-05-03 Heraeus Quarzglas Gmbh & Co. Kg Porous carbon product, method for the production thereof, and use of the same
CN103097289A (en) * 2010-10-26 2013-05-08 三井金属矿业株式会社 Method for producing carbon monoxide and production apparatus
WO2014042542A1 (en) * 2012-09-11 2014-03-20 Arcactive Limited Method of manufacturing a carbon fibre electrode of a lead-acid battery or cell

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160013497A1 (en) * 2013-03-15 2016-01-14 Graftech International Holdings Inc. Improved electrode for flow batteries
CN108461831B (en) * 2018-03-20 2020-01-14 朱玉法 Novel storage battery manufacturing method
KR102563523B1 (en) * 2020-12-29 2023-08-10 한국과학기술연구원 Method for manufacturing composite electrode for secondary battery, and composite electrode for secondary battery manufactured thereby

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3121028A (en) * 1959-06-29 1964-02-11 Ethyl Corp High performance battery
US3479151A (en) * 1966-01-03 1969-11-18 Hitco Method of carbonizing fibrous cellulosic materials
US5492782A (en) * 1994-12-06 1996-02-20 Hughes Aircraft Company Battery having fiber electrodes
US20070142225A1 (en) * 2005-12-16 2007-06-21 Baker Frederick S Activated carbon fibers and engineered forms from renewable resources

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3374445B2 (en) * 1992-10-05 2003-02-04 新神戸電機株式会社 Plate for lead-acid battery
US5858530A (en) * 1996-04-25 1999-01-12 Mccullough, Jr.; Francis P. Flexible ignition resistant biregional fiber, articles made from biregional fibers, and method of manufacture
US7105252B2 (en) * 2002-05-22 2006-09-12 Firefly Energy, Inc. Carbon coated battery electrodes
US6783851B2 (en) * 2002-08-07 2004-08-31 Albany International Techniweave, Inc. Pitch based graphite fabrics and needled punched felts for fuel cell gas diffusion layer substrates and high thermal conductivity reinforced composites
EP1550766A4 (en) * 2002-09-25 2009-07-22 Mitsubishi Chem Corp Carbonaceous fiber fabric, roll of carbonaceous fiber fabric, gas diffusion layer material for solid polymer fuel cell, method for production of carbonaceous fiber fabric, and method for production of solid polymer fuel cell
KR101528940B1 (en) * 2006-12-27 2015-06-15 에버레디 배터리 컴퍼니, 인크. Process for making a catalytic electrode and electrochemical cell using the electrode

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3121028A (en) * 1959-06-29 1964-02-11 Ethyl Corp High performance battery
US3479151A (en) * 1966-01-03 1969-11-18 Hitco Method of carbonizing fibrous cellulosic materials
US5492782A (en) * 1994-12-06 1996-02-20 Hughes Aircraft Company Battery having fiber electrodes
US20070142225A1 (en) * 2005-12-16 2007-06-21 Baker Frederick S Activated carbon fibers and engineered forms from renewable resources

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012055731A1 (en) * 2010-10-25 2012-05-03 Heraeus Quarzglas Gmbh & Co. Kg Porous carbon product, method for the production thereof, and use of the same
CN103168002A (en) * 2010-10-25 2013-06-19 赫罗伊斯石英玻璃股份有限两合公司 Porous carbon product, method for the production thereof, and use of the same
US9287556B2 (en) 2010-10-25 2016-03-15 Heraeus Quarzglas Gmbh & Co. Kg Porous carbon product, method for the production thereof, and use of the same
CN103097289A (en) * 2010-10-26 2013-05-08 三井金属矿业株式会社 Method for producing carbon monoxide and production apparatus
WO2014042542A1 (en) * 2012-09-11 2014-03-20 Arcactive Limited Method of manufacturing a carbon fibre electrode of a lead-acid battery or cell

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