CA2408618A1 - Electrochemical double layer capacitor having carbon powder electrodes - Google Patents
Electrochemical double layer capacitor having carbon powder electrodes Download PDFInfo
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- CA2408618A1 CA2408618A1 CA002408618A CA2408618A CA2408618A1 CA 2408618 A1 CA2408618 A1 CA 2408618A1 CA 002408618 A CA002408618 A CA 002408618A CA 2408618 A CA2408618 A CA 2408618A CA 2408618 A1 CA2408618 A1 CA 2408618A1
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title abstract description 124
- 239000003990 capacitor Substances 0.000 title abstract description 91
- 238000000576 coating method Methods 0.000 abstract description 72
- 239000011248 coating agent Substances 0.000 abstract description 54
- 239000002002 slurry Substances 0.000 abstract description 47
- 239000011888 foil Substances 0.000 abstract description 16
- 239000011230 binding agent Substances 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000002904 solvent Substances 0.000 abstract description 7
- 229910052799 carbon Inorganic materials 0.000 description 29
- 238000000034 method Methods 0.000 description 21
- 239000008151 electrolyte solution Substances 0.000 description 18
- 239000003792 electrolyte Substances 0.000 description 17
- 239000000843 powder Substances 0.000 description 17
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- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 9
- 229910052782 aluminium Inorganic materials 0.000 description 9
- 239000002987 primer (paints) Substances 0.000 description 9
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- 229920005596 polymer binder Polymers 0.000 description 8
- 239000002491 polymer binding agent Substances 0.000 description 8
- 239000011148 porous material Substances 0.000 description 8
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- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
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- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
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- 230000002411 adverse Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 description 1
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- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000011255 nonaqueous electrolyte Substances 0.000 description 1
- 239000012457 nonaqueous media Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- CBXCPBUEXACCNR-UHFFFAOYSA-N tetraethylammonium Chemical group CC[N+](CC)(CC)CC CBXCPBUEXACCNR-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/10—Multiple hybrid or EDL capacitors, e.g. arrays or modules
- H01G11/12—Stacked hybrid or EDL capacitors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/26—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features
- H01G11/28—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features arranged or disposed on a current collector; Layers or phases between electrodes and current collectors, e.g. adhesives
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
- H01G11/34—Carbon-based characterised by carbonisation or activation of carbon
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/66—Current collectors
- H01G11/72—Current collectors specially adapted for integration in multiple or stacked hybrid or EDL capacitors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/84—Processes for the manufacture of hybrid or EDL capacitors, or components thereof
- H01G11/86—Processes for the manufacture of hybrid or EDL capacitors, or components thereof specially adapted for electrodes
-
- 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
- Y02E60/13—Energy storage using capacitors
Abstract
A double layer capacitor (Figure 1) includes first (12) and second (14) electrode structures separated by a porous each include a current collector foil (22), a primary coating formed on the current collector foil, and a secondary coating formed on the primary coating. The primary coatings include conducting carbon powder (42), and the secondary coatings include activated carbon powder (44). A method of making the electrode structures includes the steps of : preparing a first slurry that includes conducting carbon powder and a binder; applying the first slurry to form a primary coating; preparing a second slurry that includes activated carbon powder, a solvent and a binder;
and applying the second slurry to the primary coating.
and applying the second slurry to the primary coating.
Description
ELECTROCHEMICAL DOUBLE LAYER
CAPACITOR HAVING CARBON POWDER ELECTRODES
HACRGROUND OF THE INVENTION
The present invention relates generally to electric double layer capacitors, and more particularly to a high performance double layer capacitor made with low-resistance carbon powder electrodes.
.0 Double layer capacitors, also referred to as electrochemical double layer capacitors (EDLC), are energy storage devices that are able to store more energy per unit weight and unit volume than traditional capacitors. In addition, they can typically deliver the .5 stored energy at a higher power rating than rechargeable batteries.
Double layer capacitors consist of two porous electrodes that are isolated from electrical contact by a porous separator. Both the separator and the electrodes .0 are impregnated with an electrolytic solution. This allows ionic current to flow between the electrodes through the separator at the same time that the separator prevents an electrical or electronic (as opposed to an ionic) current~from shorting the cell. Coupled to the .5 back of each of the active electrodes is a current collecting plate. One purpose of the current collecting plate is to reduce ohmic losses in the double layer capacitor. If these current collecting plates are non-porous, they can also be used as part of the .0 capacitor seal.
Double layer capacitors store electrostatic energy in a polarized liquid layer which forms when a potential exists between two electrodes immersed in an electrolyte. When the potential is applied across the .5 electrodes, a double layer of positive arid negative charges is formed at the electrode-electrolyte interface
CAPACITOR HAVING CARBON POWDER ELECTRODES
HACRGROUND OF THE INVENTION
The present invention relates generally to electric double layer capacitors, and more particularly to a high performance double layer capacitor made with low-resistance carbon powder electrodes.
.0 Double layer capacitors, also referred to as electrochemical double layer capacitors (EDLC), are energy storage devices that are able to store more energy per unit weight and unit volume than traditional capacitors. In addition, they can typically deliver the .5 stored energy at a higher power rating than rechargeable batteries.
Double layer capacitors consist of two porous electrodes that are isolated from electrical contact by a porous separator. Both the separator and the electrodes .0 are impregnated with an electrolytic solution. This allows ionic current to flow between the electrodes through the separator at the same time that the separator prevents an electrical or electronic (as opposed to an ionic) current~from shorting the cell. Coupled to the .5 back of each of the active electrodes is a current collecting plate. One purpose of the current collecting plate is to reduce ohmic losses in the double layer capacitor. If these current collecting plates are non-porous, they can also be used as part of the .0 capacitor seal.
Double layer capacitors store electrostatic energy in a polarized liquid layer which forms when a potential exists between two electrodes immersed in an electrolyte. When the potential is applied across the .5 electrodes, a double layer of positive arid negative charges is formed at the electrode-electrolyte interface
2 (henc,e, the name "double layer" capacitor) by the polarization of the electrolyte ions due to charge separation under the applied electric field, and also due to the dipole orientation and alignment of electrolyte molecules over the entire surface of the electrodes.
The use of carbon electrodes in electrochemical capacitors with high power and energy density represents a significant advantage in this technology because carbon has a low density and carbon electrodes can be fabricated with very high surface areas. Fabrication of double layer capacitors with carbon electrodes has been known in the art for quite some time, as evidenced by U.S. Pat.
Nos. 2,800,616 (Becker), and 3,648,126 (Boos et al.).
A major problem in many carbon electrode capacitors, including double layer capacitors, is that the performance of the capacitor is often limited because of the high internal resistance of the carbon electrodes.
This high internal resistance may be due to several factors, including the high contact resistance of the internal carbon-carbon contacts, and the contact resistance of the electrodes with a current collector.
This high resistance translates to large ohmic losses in the capacitor during the charging and discharge phases, which losses further adversely affect the characteristic RC (resistance times capacitance) time constant of the capacitor and interfere with its ability to be efficiently charged and/or discharged in a short period of time. There is thus a need in the art for lowering the internal resistance, and hence the time constant, of double layer capacitors.
United States Patent No. 5,907,472 to Farahmandi et al., the complete disclosure of which is incorporated herein by reference, discloses a multi-electrode double layer capacitor having a single electrolyte seal and aluminum-impregnated carbon cloth electrodes. The use of the aluminum-impregnated carbon cloth electrodes. described therein results in a double
The use of carbon electrodes in electrochemical capacitors with high power and energy density represents a significant advantage in this technology because carbon has a low density and carbon electrodes can be fabricated with very high surface areas. Fabrication of double layer capacitors with carbon electrodes has been known in the art for quite some time, as evidenced by U.S. Pat.
Nos. 2,800,616 (Becker), and 3,648,126 (Boos et al.).
A major problem in many carbon electrode capacitors, including double layer capacitors, is that the performance of the capacitor is often limited because of the high internal resistance of the carbon electrodes.
This high internal resistance may be due to several factors, including the high contact resistance of the internal carbon-carbon contacts, and the contact resistance of the electrodes with a current collector.
This high resistance translates to large ohmic losses in the capacitor during the charging and discharge phases, which losses further adversely affect the characteristic RC (resistance times capacitance) time constant of the capacitor and interfere with its ability to be efficiently charged and/or discharged in a short period of time. There is thus a need in the art for lowering the internal resistance, and hence the time constant, of double layer capacitors.
United States Patent No. 5,907,472 to Farahmandi et al., the complete disclosure of which is incorporated herein by reference, discloses a multi-electrode double layer capacitor having a single electrolyte seal and aluminum-impregnated carbon cloth electrodes. The use of the aluminum-impregnated carbon cloth electrodes. described therein results in a double
3 layer, capacitor having a very low internal resistance.
The carbon cloth used in such electrodes, however, tends to be somewhat costly. Thus, it would be advantageous to have a method and/or apparatus for lowering the~internal resistance of double layer capacitors that does not rely on carbon cloth.
It is thus apparent that there is a continuing need for improved double layer capacitors. Such improved double layer capacitors need to deliver large amounts of useful energy at a very high power output and energy density ratings within a relatively short period of time.
Such improved double layer capacitors should also have a relatively low internal resistance and yet be capable of yielding a relatively high operating voltage.
Furthermore, it is also apparent that improvements are needed in the techniques and methods of fabricating double layer capacitor electrodes so as to lower the internal resistance of the double layer capacitor and maximize the operating voltage. For example, the method used to connect the current collector plate to the electrode is important because the interface between the electrode and the current collector plate is a source of internal° resistance of the double layer capacitor. Since capacitor energy density increases with the square of the operating voltage, higher operating voltages thus translate directly into significantly higher energy densities and, as a result, higher power output ratings. It is thus readily apparent that improved techniques and methods are needed to lower the internal resistance of the electrodes used within a double layer capacitor and increase the operating voltage.
SUMMARY OF THE INVENTION
The present invention advantageously addresses the needs above as well as other needs by providing a method of making an electrode structure for use in a
The carbon cloth used in such electrodes, however, tends to be somewhat costly. Thus, it would be advantageous to have a method and/or apparatus for lowering the~internal resistance of double layer capacitors that does not rely on carbon cloth.
It is thus apparent that there is a continuing need for improved double layer capacitors. Such improved double layer capacitors need to deliver large amounts of useful energy at a very high power output and energy density ratings within a relatively short period of time.
Such improved double layer capacitors should also have a relatively low internal resistance and yet be capable of yielding a relatively high operating voltage.
Furthermore, it is also apparent that improvements are needed in the techniques and methods of fabricating double layer capacitor electrodes so as to lower the internal resistance of the double layer capacitor and maximize the operating voltage. For example, the method used to connect the current collector plate to the electrode is important because the interface between the electrode and the current collector plate is a source of internal° resistance of the double layer capacitor. Since capacitor energy density increases with the square of the operating voltage, higher operating voltages thus translate directly into significantly higher energy densities and, as a result, higher power output ratings. It is thus readily apparent that improved techniques and methods are needed to lower the internal resistance of the electrodes used within a double layer capacitor and increase the operating voltage.
SUMMARY OF THE INVENTION
The present invention advantageously addresses the needs above as well as other needs by providing a method of making an electrode structure for use in a
4 PCT/USO1/15333 double layer capacitor. The method includes the steps of: preparing a first slurry that includes conducting carbon powder and a binder; applying the first slurry to a current collector plate; drying the applied first slurry to form a primary coating; preparing a second slurry that includes activated carbon powder, a solvent and a binder; and applying the second slurry to the primary coating.
The present invention also provides a double layer capacitor that includes first and second electrode structures, a porous separator, and a saturation means.
The first electrode structure includes a first current collector foil, a first primary coating formed on the first current collector foil, and a first secondary coating formed on the first primary coating. The second electrode structure includes a second current collector foil, a second primary coating formed on the second current collector foil, and a second secondary coating formed on the second primary coating. The first and second primary coatings include conducting carbon powder, and the first and second secondary coatings include activated carbon powder. The porous separator is positioned between the first and second electrodes structures. The saturation means saturates the porous separator and the first and second electrodes structures in a prescribed electrolytic solution.
A better understanding of the features and advantages of the present invention will be obtained by reference to the following detailed description of the invention and accompanying drawings which set forth an illustrative embodiment in which the principles of the invention are utilized.
BRIEF DESCRIPTION OF THE DRAWINGS
The above and other aspects, features and.
advantages of the present invention will be more apparent from the following more particular description thereof presented in conjunction with the following drawings herein;
FIG. 1 is a schematic diagram illustrating a double layer capacitor made in accordance with the
The present invention also provides a double layer capacitor that includes first and second electrode structures, a porous separator, and a saturation means.
The first electrode structure includes a first current collector foil, a first primary coating formed on the first current collector foil, and a first secondary coating formed on the first primary coating. The second electrode structure includes a second current collector foil, a second primary coating formed on the second current collector foil, and a second secondary coating formed on the second primary coating. The first and second primary coatings include conducting carbon powder, and the first and second secondary coatings include activated carbon powder. The porous separator is positioned between the first and second electrodes structures. The saturation means saturates the porous separator and the first and second electrodes structures in a prescribed electrolytic solution.
A better understanding of the features and advantages of the present invention will be obtained by reference to the following detailed description of the invention and accompanying drawings which set forth an illustrative embodiment in which the principles of the invention are utilized.
BRIEF DESCRIPTION OF THE DRAWINGS
The above and other aspects, features and.
advantages of the present invention will be more apparent from the following more particular description thereof presented in conjunction with the following drawings herein;
FIG. 1 is a schematic diagram illustrating a double layer capacitor made in accordance with the
5 present invention;
FIG. 2 is a schematic diagram illustrating a multi-electrode double layer capacitor made in accordance with the present invention;
FIG. 3 is a flowchart illustrating an exemplars process in accordance with the present invention for making the carbon powder electrodes shown in FIGS. 1 and 2;
' FIG. 4 is a side view illustrating one of the current collector plates shown in FIG. 1;
FIG. 5 is an isometric view illustrating a process of coating the current collector plate shown in FIG. 4;
FIG. 6 is a side view illustrating the coated current collector plate resulting from the process shown in FIG. 5;
FIG. 7 is a side view illustrating a process o:
cutting the coated current collector plate shown in FIG.
FIG. 2 is a schematic diagram illustrating a multi-electrode double layer capacitor made in accordance with the present invention;
FIG. 3 is a flowchart illustrating an exemplars process in accordance with the present invention for making the carbon powder electrodes shown in FIGS. 1 and 2;
' FIG. 4 is a side view illustrating one of the current collector plates shown in FIG. 1;
FIG. 5 is an isometric view illustrating a process of coating the current collector plate shown in FIG. 4;
FIG. 6 is a side view illustrating the coated current collector plate resulting from the process shown in FIG. 5;
FIG. 7 is a side view illustrating a process o:
cutting the coated current collector plate shown in FIG.
6; and FIG. 8 is a side view illustrating a secondary coating applied to the coated current collector plate shown in FIG. 7.
Corresponding reference characters indicate corresponding components throughout several views of the drawing.
DETAINED DESCRIPTION OF THE INVENTION
The following description of the presently contemplated best mode of practicing the invention is no to be taken in a limiting sense, but is made merely for the purpose of describing the general principle of the invention. The scope of the invention should be determined with reference to the claims.
Activated carbon powders can be used to provide high capacitance in electrochemical double-,layer capacitors (EDLC). A high capacitance is possible due to the large surface area of activated carbon, which is on the order of 1000 to 2500 m~/g.
One possible method of making carbon powder electrodes is to apply the activated carbon powders onto current collectors in the form of a slurry. Such a slurry of activated carbon powder may be made in a solution containing a polymer binder. The resultant electrodes, however, tend to be resistive. To partially alleviate this problem, a small percentage (e.g., 1-2%) of a carbon, which is more conducting than the activated carbon, may be added to the slurry. Thus, the electrodes are made by applying a single coat of activated carbon, conducting carbon, and a polymer binder onto current collectors. Unfortunately, the time constants of EDLC
capacitors having these types of electrodes typically fall in the range of 3-5 seconds,. It would be highly advantageous to produce EDLC capacitors having lower time constants.
Referring to FIG. 1, there is illustrated a schematic representation of a two-electrode single cell double layer capacitor 100 made in accordance with~the present invention. The capacitor 100 has a very low internal resistance and is capable of yielding a high operating voltage. Furthermore, the capacitor 100 is capable of achieving an RC time constant of 0.5 seconds.
The capacitor 100 includes two spaced apart carbon powder electrodes 102, 104 electrically separated by a porous separator 106. One purpose of the electronic separator 106 is to assure that the opposing electrodes 102, 104 are never in contact with one another. Contact between electrodes results in a short circuit and rapid depletion of the charges stored in the electrodes.
The first electrode 102 is in contact with a current collector plate 108, which plate 108 is in turn
Corresponding reference characters indicate corresponding components throughout several views of the drawing.
DETAINED DESCRIPTION OF THE INVENTION
The following description of the presently contemplated best mode of practicing the invention is no to be taken in a limiting sense, but is made merely for the purpose of describing the general principle of the invention. The scope of the invention should be determined with reference to the claims.
Activated carbon powders can be used to provide high capacitance in electrochemical double-,layer capacitors (EDLC). A high capacitance is possible due to the large surface area of activated carbon, which is on the order of 1000 to 2500 m~/g.
One possible method of making carbon powder electrodes is to apply the activated carbon powders onto current collectors in the form of a slurry. Such a slurry of activated carbon powder may be made in a solution containing a polymer binder. The resultant electrodes, however, tend to be resistive. To partially alleviate this problem, a small percentage (e.g., 1-2%) of a carbon, which is more conducting than the activated carbon, may be added to the slurry. Thus, the electrodes are made by applying a single coat of activated carbon, conducting carbon, and a polymer binder onto current collectors. Unfortunately, the time constants of EDLC
capacitors having these types of electrodes typically fall in the range of 3-5 seconds,. It would be highly advantageous to produce EDLC capacitors having lower time constants.
Referring to FIG. 1, there is illustrated a schematic representation of a two-electrode single cell double layer capacitor 100 made in accordance with~the present invention. The capacitor 100 has a very low internal resistance and is capable of yielding a high operating voltage. Furthermore, the capacitor 100 is capable of achieving an RC time constant of 0.5 seconds.
The capacitor 100 includes two spaced apart carbon powder electrodes 102, 104 electrically separated by a porous separator 106. One purpose of the electronic separator 106 is to assure that the opposing electrodes 102, 104 are never in contact with one another. Contact between electrodes results in a short circuit and rapid depletion of the charges stored in the electrodes.
The first electrode 102 is in contact with a current collector plate 108, which plate 108 is in turn
7 connected to a first electrical terminal 110 of the capacitor 100. Similarly,' the second electrode 104 is in contact with another current collector plate 112, which plate 112 is connected to a second electrical terminal 114 of the capacitor 100. The current collector plates 108, 112 preferably comprise aluminum foil or the like.
The region between the electrodes 102, 104, as well as all of the available spaces and voids within the electrodes 102, 104, are filled with a highly conductive, preferably non-aqueous electrolytic solution 116.
The electrodes 102, 104, as explained in more detail below, are preferably formed by~applying two different types of carbon powder slurries to the current collector plates 108, 112 in two separate coatings.
Specifically, the first electrode 102 includes a primary (or primer) coating 120 that is in contact with the current collector plate 108. Similarly, the second electrode 104 includes a primary (or primer) coating 122 that is in contact with the current collector plate 112.
The primary coatings 120, 122 preferably comprise a carbon powder film that contains highly conducting carbon powder in large proportion and a polymer binder. The proportion of highly conducting carbon included in the primary coatings 120, 122 preferably falls in the range of 25%-95%. The primary coatings 120, 122 preferably do not contain activated carbon.
The first electrode 102 also includes a secondary coating 124, and similarly, the second electrode 104 includes a secondary coating 126. The secondary coatings 124, 126 are both in contact with the separator 106. The secondary coatings 124, 126 are applied on top of the primary coatings 120, 122, respectively, and are preferably applied with slurry of activated carbon, conducting carbon and a polymer binder.
The illustrated components are compressed against each other with a constant modest pressure, with the porous separator 106~preventing an electrical short between the
The region between the electrodes 102, 104, as well as all of the available spaces and voids within the electrodes 102, 104, are filled with a highly conductive, preferably non-aqueous electrolytic solution 116.
The electrodes 102, 104, as explained in more detail below, are preferably formed by~applying two different types of carbon powder slurries to the current collector plates 108, 112 in two separate coatings.
Specifically, the first electrode 102 includes a primary (or primer) coating 120 that is in contact with the current collector plate 108. Similarly, the second electrode 104 includes a primary (or primer) coating 122 that is in contact with the current collector plate 112.
The primary coatings 120, 122 preferably comprise a carbon powder film that contains highly conducting carbon powder in large proportion and a polymer binder. The proportion of highly conducting carbon included in the primary coatings 120, 122 preferably falls in the range of 25%-95%. The primary coatings 120, 122 preferably do not contain activated carbon.
The first electrode 102 also includes a secondary coating 124, and similarly, the second electrode 104 includes a secondary coating 126. The secondary coatings 124, 126 are both in contact with the separator 106. The secondary coatings 124, 126 are applied on top of the primary coatings 120, 122, respectively, and are preferably applied with slurry of activated carbon, conducting carbon and a polymer binder.
The illustrated components are compressed against each other with a constant modest pressure, with the porous separator 106~preventing an electrical short between the
8 electrodes 102, 104.
The electrodes 10,2, 104, with their primary coatings 120, 122 and secondary coatings 124, 126, have lower resistance than electrodes made with a single coat of activated carbon, conducting carbon, and a polymer binder as described above.
The ions of the electrolytic solution 116 are free to pass through pores or holes 118 of the separator 106; yet the separator 106 prevents the electrode 102 from physically contacting, and hence electrically shorting with, the electrode 104. A preferred separator 106, for example, is polypropylene. Polypropylene includes rectangular-shaped pore openings having dimensions on the order of 0.04 by 0.12 ~.m. Another suitable separator material is polyethylene.
Polyethylene generally has pore sizes on the order of 0..
~m diameter or less.
In operation, when an electrical potential is applied across the terminals 110, 114, and hence across the series-connected electrodes 102, 104, a polarized liquid layer forms at each electrode immersed in the electrolyte 116. It is these polarized liquid layers which store electrostatic energy and function as the double layer capacitor--i.e., that function as two capacitors in series.
More specifically, as conceptually depicted by the "+" and "-" symbols (representing the electrical charge at the electrode-electrolyte interface of each electrode that is immersed in the electrolyte 116), when a voltage is applied across the electrodes, e.g., when electrode 102 is charged positive relative to electrode 104, a double layer is formed (symbolically depicted by the two "+/-" layers) by the polarization of the electrolyte ions due to charge separation under the applied electric field and also due to the dipole orientation and alignment of electrolyte molecules over the entire surface of the electrodes. This polarization
The electrodes 10,2, 104, with their primary coatings 120, 122 and secondary coatings 124, 126, have lower resistance than electrodes made with a single coat of activated carbon, conducting carbon, and a polymer binder as described above.
The ions of the electrolytic solution 116 are free to pass through pores or holes 118 of the separator 106; yet the separator 106 prevents the electrode 102 from physically contacting, and hence electrically shorting with, the electrode 104. A preferred separator 106, for example, is polypropylene. Polypropylene includes rectangular-shaped pore openings having dimensions on the order of 0.04 by 0.12 ~.m. Another suitable separator material is polyethylene.
Polyethylene generally has pore sizes on the order of 0..
~m diameter or less.
In operation, when an electrical potential is applied across the terminals 110, 114, and hence across the series-connected electrodes 102, 104, a polarized liquid layer forms at each electrode immersed in the electrolyte 116. It is these polarized liquid layers which store electrostatic energy and function as the double layer capacitor--i.e., that function as two capacitors in series.
More specifically, as conceptually depicted by the "+" and "-" symbols (representing the electrical charge at the electrode-electrolyte interface of each electrode that is immersed in the electrolyte 116), when a voltage is applied across the electrodes, e.g., when electrode 102 is charged positive relative to electrode 104, a double layer is formed (symbolically depicted by the two "+/-" layers) by the polarization of the electrolyte ions due to charge separation under the applied electric field and also due to the dipole orientation and alignment of electrolyte molecules over the entire surface of the electrodes. This polarization
9 stores energy in the capacitor according to the following relationships:
C=keA/ d ( 1 ) and E=CVZ / 2 ( 2 ) where C is the capacitance, ke is the effective dielectri constant of the double layer, d is the separation distance between the layers, A is the surface area of the electrodes that is immersed in the electrolytic solution, V is the voltage applied across the electrodes, and E is the energy stored in the capacitor.
In a double layer capacitor, the separation distance d is so small that it is measured in angstroms,.
while the surface area A, i.e., the surface area "A" per gram of electrode material, may be very large. Hence, a:
can be seen from Eq. (1), when d is very small, and A is very large, the capacitance will be very large.
The surface area "A" in the capacitor 100 is large because of the make-up of the electrodes 102, 104.
Specifically, each of the electrodes 102, 104 comprises activated carbon powders in the secondary coatings 124, 126, respectively. Activated carbon is a highly porous form of carbon. The activated carbon powders do not havE
a smooth surface, but are pitted with numerous holes and pores. The holes and pores of the activated carbon powders have a typical size of about 10-100 A
(Angstroms). The powders are immersed in the electrolytic solution 116. Each hole and pore significantly increases the surface area of the powder that is exposed to the electrolytic solution 116. The result is a three-dimensional electrode structure which allows the electrolyte to penetrate into the holes and contact all, or most all, of the surface area of the carboy powders, thereby dramatically increasing the surface area "A" of the electrode over which the double layer of charged molecules is formed.
Achieving a high capacitance, however, is only 5 part of the invention. The capacitor 100 is also capable of storing and discharging energy in a relatively quick time period. In general, the charge/discharge time of a capacitor is governed by the internal resistance of the capacitor. The lower the internal resistance, the
C=keA/ d ( 1 ) and E=CVZ / 2 ( 2 ) where C is the capacitance, ke is the effective dielectri constant of the double layer, d is the separation distance between the layers, A is the surface area of the electrodes that is immersed in the electrolytic solution, V is the voltage applied across the electrodes, and E is the energy stored in the capacitor.
In a double layer capacitor, the separation distance d is so small that it is measured in angstroms,.
while the surface area A, i.e., the surface area "A" per gram of electrode material, may be very large. Hence, a:
can be seen from Eq. (1), when d is very small, and A is very large, the capacitance will be very large.
The surface area "A" in the capacitor 100 is large because of the make-up of the electrodes 102, 104.
Specifically, each of the electrodes 102, 104 comprises activated carbon powders in the secondary coatings 124, 126, respectively. Activated carbon is a highly porous form of carbon. The activated carbon powders do not havE
a smooth surface, but are pitted with numerous holes and pores. The holes and pores of the activated carbon powders have a typical size of about 10-100 A
(Angstroms). The powders are immersed in the electrolytic solution 116. Each hole and pore significantly increases the surface area of the powder that is exposed to the electrolytic solution 116. The result is a three-dimensional electrode structure which allows the electrolyte to penetrate into the holes and contact all, or most all, of the surface area of the carboy powders, thereby dramatically increasing the surface area "A" of the electrode over which the double layer of charged molecules is formed.
Achieving a high capacitance, however, is only 5 part of the invention. The capacitor 100 is also capable of storing and discharging energy in a relatively quick time period. In general, the charge/discharge time of a capacitor is governed by the internal resistance of the capacitor. The lower the internal resistance, the
10 shorter the charge/discharge time.
The internal resistance of the basic double layer capacitor 100 is made up of several components.
Specifically, the internal resistance components include a contact resistance R~, an electrode resistance REL, an electrolytic solution resistance RES, and a separator resistance RSEp. The contact resistance R~ represents all of the resistance in the current path between the capacitor terminal 110 up to the electrode 102, or all of the resistance in the current path between the capacitor terminal 114 and the electrode 104. The electrode resistance REL represents the resistance within the electrode 102 (or within the electrode 104). The electrolytic solution resistance RES exits relative to the electrolytic solution 116, and the separator resistance RSE~ exists relative to the porous separator 106.
Any energy stored within the capacitor 100 enters or exits the capacitor by way of an electrical current that flows through R~, REL, RES, and RSEp. Thus it is seen that in order for practical charge/discharge times to be achieved, the values of R~, REL, Rasi and RSEP/
which in combination with the capacitance C define the time constant z~ of the capacitor 100, are preferably kepi as low as possible.
The resistance of the separator RSEp is a function of the porosity and thickness of the separator 106. A preferred separator material is polypropylene having a thickness of about 0.001 inches (0.025 mm). An
The internal resistance of the basic double layer capacitor 100 is made up of several components.
Specifically, the internal resistance components include a contact resistance R~, an electrode resistance REL, an electrolytic solution resistance RES, and a separator resistance RSEp. The contact resistance R~ represents all of the resistance in the current path between the capacitor terminal 110 up to the electrode 102, or all of the resistance in the current path between the capacitor terminal 114 and the electrode 104. The electrode resistance REL represents the resistance within the electrode 102 (or within the electrode 104). The electrolytic solution resistance RES exits relative to the electrolytic solution 116, and the separator resistance RSE~ exists relative to the porous separator 106.
Any energy stored within the capacitor 100 enters or exits the capacitor by way of an electrical current that flows through R~, REL, RES, and RSEp. Thus it is seen that in order for practical charge/discharge times to be achieved, the values of R~, REL, Rasi and RSEP/
which in combination with the capacitance C define the time constant z~ of the capacitor 100, are preferably kepi as low as possible.
The resistance of the separator RSEp is a function of the porosity and thickness of the separator 106. A preferred separator material is polypropylene having a thickness of about 0.001 inches (0.025 mm). An
11 alternative separator material is polyethylene, also having a thickness of about 0.001 inches (0.025 mm).
Polypropylene inherently has larger pores than does polyethylene due the manner in which polypropylene is constructed. Polypropylene typically exhibits a porosity of 25-40%; whereas polyethylene exhibits a porosity of 40-60%. Hence, polyethylene inherently demonstrates a lower separator resistance than does polypropylene simply because it has a higher porosity, i.e, there are more pores or openings through which the electrolyte ions may flow, even though the holes are, on average, smaller. In addition, a paper separator may also be used.
The resistance RES relative to the electrolytic solution 116 is determined by the conductivity of the particular electrolytic solution that is used. In selecting the type of electrolytic solution to use, several tradeoffs are considered. Aqueous electrolytic solutions generally have a higher conductivity than do non-aqueous solutions (e. g., by a factor of 10).
However, aqueous solutions limit the working voltage of the capacitor cell to around 0.5 to 1.0 volt. Because the energy stored in the cell is a function of the square of the voltage, high energy applications are probably better served using a non-aqueous electrolyte, which permit cell voltages on the order of 2.0 to 3.0 volts.
One preferred electrolyte 116 for use with the double layer capacitor 100 described herein is made from a mixture of acetonitrile (CH3CN) and a suitable salt, whict mixture exhibits a conductivity on the order of 60 ohzril cm 1. By way of example, one suitable salt is tetra ethylammonium tetra fluoriborate (EtdNBF4). It is to be emphasized, however, that the invention herein described contemplates the use of alternate electrolytic solutions, particularly non-aqueous (or organic) electrolytic solutions, other than the solution made from acetonitrile described above. By way of example, possible solvents include propylene carbonate (PC), ethylmethyl carbonate
Polypropylene inherently has larger pores than does polyethylene due the manner in which polypropylene is constructed. Polypropylene typically exhibits a porosity of 25-40%; whereas polyethylene exhibits a porosity of 40-60%. Hence, polyethylene inherently demonstrates a lower separator resistance than does polypropylene simply because it has a higher porosity, i.e, there are more pores or openings through which the electrolyte ions may flow, even though the holes are, on average, smaller. In addition, a paper separator may also be used.
The resistance RES relative to the electrolytic solution 116 is determined by the conductivity of the particular electrolytic solution that is used. In selecting the type of electrolytic solution to use, several tradeoffs are considered. Aqueous electrolytic solutions generally have a higher conductivity than do non-aqueous solutions (e. g., by a factor of 10).
However, aqueous solutions limit the working voltage of the capacitor cell to around 0.5 to 1.0 volt. Because the energy stored in the cell is a function of the square of the voltage, high energy applications are probably better served using a non-aqueous electrolyte, which permit cell voltages on the order of 2.0 to 3.0 volts.
One preferred electrolyte 116 for use with the double layer capacitor 100 described herein is made from a mixture of acetonitrile (CH3CN) and a suitable salt, whict mixture exhibits a conductivity on the order of 60 ohzril cm 1. By way of example, one suitable salt is tetra ethylammonium tetra fluoriborate (EtdNBF4). It is to be emphasized, however, that the invention herein described contemplates the use of alternate electrolytic solutions, particularly non-aqueous (or organic) electrolytic solutions, other than the solution made from acetonitrile described above. By way of example, possible solvents include propylene carbonate (PC), ethylmethyl carbonate
12 (EMC), ethylene carbonate (EC), dimethyl carbonate (DMC), and their mixtures.
The contact resistance R~ in combination with the electrode resistance REL represent a significant portion of the total internal resistance of the capacitor 100. A high electrode resistance has heretofore been ae major stumbling block in the development of commercially viable, high energy density, double layer capacitors. A
key feature of the present invention is to provide a double layer capacitor having a very low electrode resistance in combination with a high energy density. A
result of the present invention is that R~+REL are reduced to a value that is small in comparison to RSEp+ RES~
The unique structure of the electrodes 102, 109 described herein contributes to the electrode resistance REL being very small. Specifically, the large proportion of highly conducting carbon powder and the lack of activated carbon in the primary coatings 120, 122 significantly reduces the total electrode resistance REL~
This is because the interface resistance between the primary coating 120 (or 122) and the collector plate 108 (or 112) is extremely low due to the highly conducting carbon powder. Furthermore, the interface resistance between the primary coating 120 (or 122) and the secondary coating 124 (or 126) is also extremely low due to carbon/carbon interface. Because of the intimate mixing of the primary coating 120 (or 122) and the secondary coating 124 (or 126), the interface area of the primary coating and the secondary coating is higher.
This increased interface area establishes a greater number of conducting paths for the activated carbon than would otherwise be possible without the primary coatings 120, 122. This increased number of conducting paths decreases the resistance.
An important aspect of the present invention, as will. become more apparent from the description that follows, is the use of multiple carbon powder electrodes
The contact resistance R~ in combination with the electrode resistance REL represent a significant portion of the total internal resistance of the capacitor 100. A high electrode resistance has heretofore been ae major stumbling block in the development of commercially viable, high energy density, double layer capacitors. A
key feature of the present invention is to provide a double layer capacitor having a very low electrode resistance in combination with a high energy density. A
result of the present invention is that R~+REL are reduced to a value that is small in comparison to RSEp+ RES~
The unique structure of the electrodes 102, 109 described herein contributes to the electrode resistance REL being very small. Specifically, the large proportion of highly conducting carbon powder and the lack of activated carbon in the primary coatings 120, 122 significantly reduces the total electrode resistance REL~
This is because the interface resistance between the primary coating 120 (or 122) and the collector plate 108 (or 112) is extremely low due to the highly conducting carbon powder. Furthermore, the interface resistance between the primary coating 120 (or 122) and the secondary coating 124 (or 126) is also extremely low due to carbon/carbon interface. Because of the intimate mixing of the primary coating 120 (or 122) and the secondary coating 124 (or 126), the interface area of the primary coating and the secondary coating is higher.
This increased interface area establishes a greater number of conducting paths for the activated carbon than would otherwise be possible without the primary coatings 120, 122. This increased number of conducting paths decreases the resistance.
An important aspect of the present invention, as will. become more apparent from the description that follows, is the use of multiple carbon powder electrodes
13 connected in parallel within a capacitor package that requires only a single electrolyte seal. One example configuration for parallel connected multiple carbon powder electrodes is a "flat stack" of electrodes. It should be well understood, however, that there are many other configurations for parallel connected multiple carbon powder electrodes that may be used in accordance with the present invention. Because only one electrolyte seal is required, it is appropriate to refer to such capacitor as a "single cell" capacitor since it is the electrolyte seal which normally defines what comprises a cell. Such a single cell, multi-electrode double layer capacitor configuration is a preferred way of practicing the invention at the present time. It is to be emphasized, however, that the invention is not intended to be limited to such mode or embodiment. Rather, it is contemplated that the invention extend to all double layer capacitors that use low-resistance carbon powder electrodes in accordance with the present invention, regardless of the specific electrode configuration that may eventually be used to make the capacitor, and regardless of the specific high conductivity electrolytic solution that is employed. Such electrode configurations may include, e.g., multiple electrodes connected in parallel in a single cell (as is described more fully herein); a pair of electrodes arranged in a spiral pattern in a single cell; electrodes connected in series in stacked cells; or other electrode configurations.
Referring to FIG. 2, there is illustrated a schematic representation of a multiple-electrode single cell double layer capacitor 200 made in accordance with the present invention. The capacitor 200 comprises a structure of the components from several of the two-electrode double layer capacitors 100 described above.
The current collector plates 108 are connected in parallel to a first electrical terminal 202 of the capacitor 200, and the current collector plates 112 are
Referring to FIG. 2, there is illustrated a schematic representation of a multiple-electrode single cell double layer capacitor 200 made in accordance with the present invention. The capacitor 200 comprises a structure of the components from several of the two-electrode double layer capacitors 100 described above.
The current collector plates 108 are connected in parallel to a first electrical terminal 202 of the capacitor 200, and the current collector plates 112 are
14 connected in parallel to a second electrical terminal 204 of the capacitor 200. The electrodes associated with the first terminal 202 comprise a first set of electrodes, and the electrodes associated with the second terminal 204 comprise a second set of electrodes. The individual electrodes of the first set are interleaved with the .
individual electrodes of the second set. The porous separators 106 prevent electrical shorting between the interleaved individual electrodes. As mentioned above, the current collector plates 108, 1I2 preferably comprise aluminum foil or the like. The electrodes 102, 104 comprise the two-coating (or two-layer) carbon powder electrodes described above.
The first and second sets of electrodes in the capacitor 200 may comprise many different physical configurations. For example, in one configuration the capacitor 200 may comprise a stacked structure. In this stacked configuration the electrodes associated with the first terminal 202 may comprise a first flat stack of electrodes and the electrodes associated with the second terminal 204 may comprise a second flat stack of electrodes. It should be well understood, however, that there are many other physical configurations for the first and second sets of electrodes in the~capacitor 200 that may be used in accordance with the present invention.
In the figure, a plurality of series connected capacitor electrode pairs A, B, C, D and E are identified within the electrode structure which forms the capacitor 200. Fewer or more of the electrode pairs may be included. Each electrode pair includes a pair of carbon powder electrodes 102, 104 which are preferably fabricated as described herein. Pair A includes electrodes 102 and 104 facing one another with the ionically conductive separator 106 disposed between them.
Similarly, pairs B, C, D and E each include electrodes 102 and 104 facing one another with ionically conductive separators 106 disposed between them.
The internal non=porous current collector plates 108, 112 are placed between each electrode pair in the illustrated manner. Each of the current collector 5 plates 108, 112 has two adjoining polarized electrodes on each side thereof. It will be appreciated that the illustrated components are compressed against each other with a constant modest pressure, with the porous separators 106 preventing an electrical short between the 10 electrodes 102, 104. A sufficient amount of a highly conductive, preferably non-aqueous electrolytic solution is introduced into the cell such that the electrolyte saturates all of the electrodes 102, 104 and separators 106 within each pair.
individual electrodes of the second set. The porous separators 106 prevent electrical shorting between the interleaved individual electrodes. As mentioned above, the current collector plates 108, 1I2 preferably comprise aluminum foil or the like. The electrodes 102, 104 comprise the two-coating (or two-layer) carbon powder electrodes described above.
The first and second sets of electrodes in the capacitor 200 may comprise many different physical configurations. For example, in one configuration the capacitor 200 may comprise a stacked structure. In this stacked configuration the electrodes associated with the first terminal 202 may comprise a first flat stack of electrodes and the electrodes associated with the second terminal 204 may comprise a second flat stack of electrodes. It should be well understood, however, that there are many other physical configurations for the first and second sets of electrodes in the~capacitor 200 that may be used in accordance with the present invention.
In the figure, a plurality of series connected capacitor electrode pairs A, B, C, D and E are identified within the electrode structure which forms the capacitor 200. Fewer or more of the electrode pairs may be included. Each electrode pair includes a pair of carbon powder electrodes 102, 104 which are preferably fabricated as described herein. Pair A includes electrodes 102 and 104 facing one another with the ionically conductive separator 106 disposed between them.
Similarly, pairs B, C, D and E each include electrodes 102 and 104 facing one another with ionically conductive separators 106 disposed between them.
The internal non=porous current collector plates 108, 112 are placed between each electrode pair in the illustrated manner. Each of the current collector 5 plates 108, 112 has two adjoining polarized electrodes on each side thereof. It will be appreciated that the illustrated components are compressed against each other with a constant modest pressure, with the porous separators 106 preventing an electrical short between the 10 electrodes 102, 104. A sufficient amount of a highly conductive, preferably non-aqueous electrolytic solution is introduced into the cell such that the electrolyte saturates all of the electrodes 102, 104 and separators 106 within each pair.
15 During operation, if in electrode pair A the upper electrode 102 is a negative electrode, the lower electrode 104 of pair A becomes oppositely charged, i.e., becomes a positive electrode. The same charge of electrode 104 of pair A carries over to the upper electrode 102 of pair B, i.e., electrode 102 of pair B
becomes positively charged relative to electrode 102 of pair A. This causes the lower electrode 104 of pair B to become oppositely charged, i.e., negatively charged relative to electrode 102 of pair B. The electrodes of pairs C, D, E become charged in a similar manner.
As mentioned above, the electrodes 102, 104 are preferably formed by applying two different types of carbon powder slurries to the current collector plates 108, 112 in two separate coatings. Alternatively, the electrodes 102, 104 may be formed by forming two different carbon powder laminated films to the current collector plates 108, 112 instead of using slurries.
With respect to the carbon powder slurry technique, FIG.
3 illustrates an exemplary process 300 in accordance with the present invention that may be used for making the carbon powder electrodes of the capacitor 100 and/or 200.
The exemplary process 300 begins in step 302 by
becomes positively charged relative to electrode 102 of pair A. This causes the lower electrode 104 of pair B to become oppositely charged, i.e., negatively charged relative to electrode 102 of pair B. The electrodes of pairs C, D, E become charged in a similar manner.
As mentioned above, the electrodes 102, 104 are preferably formed by applying two different types of carbon powder slurries to the current collector plates 108, 112 in two separate coatings. Alternatively, the electrodes 102, 104 may be formed by forming two different carbon powder laminated films to the current collector plates 108, 112 instead of using slurries.
With respect to the carbon powder slurry technique, FIG.
3 illustrates an exemplary process 300 in accordance with the present invention that may be used for making the carbon powder electrodes of the capacitor 100 and/or 200.
The exemplary process 300 begins in step 302 by
16 obtaining a current collector plate, such as the current collector plate 112 shown in FIG. 4. The current collector plate 112 (and 108) preferably comprises aluminum foil. Other suitable materials for use as the current collector plates include copper, nickel, stainless steel foils, and any conducting current collectors.
The current collector plate 112 is first coated with the primary coating 122. The primary coating 122 comprises a carbon film containing highly conducting carbon powder in large proportion (e.g., 25%-95%) and a polymer binder. The primary coat 122 preferably does not contain activated carbon.
The primary coating 122 is preferably applied to the current collector plate 112 in the form of a slurry. The slurry used to form the primary coating 122 is prepared in step 304. By way of example, the slurry may comprise a slurry supplied by Acheson Colloids Company, Inc. of Port Huron, MI. Alternatively, the slurry used to form the primary coating 122 may be made from conducting carbon powders like acetylene black and/or graphite. For example, one exemplary slurry for the primary coating 122 can be made by mixing commercially available graphite and the binder polyvinyldiflouride (PVDF) in acetone. PVDF can be obtained from Elf Atochem Co. of France, as "Kynar", catalog no. PVDF 2801-00. By way of example, the commercially available graphite may be obtained from Timcal America of Westlake, Ohio, but it should be understood that any other type of graphite may be substituted. Preferably, the amount of conducting carbot powders used in the slurry falls in the range of 25 w% tc 95 w% ("w%" meaning percent by weight), with the remainder of the slurry consisting of the PVDF in acetone. Ideally, the composition of graphite can be between 50 w% and 95 w%.
After the slurry used to form the primary
The current collector plate 112 is first coated with the primary coating 122. The primary coating 122 comprises a carbon film containing highly conducting carbon powder in large proportion (e.g., 25%-95%) and a polymer binder. The primary coat 122 preferably does not contain activated carbon.
The primary coating 122 is preferably applied to the current collector plate 112 in the form of a slurry. The slurry used to form the primary coating 122 is prepared in step 304. By way of example, the slurry may comprise a slurry supplied by Acheson Colloids Company, Inc. of Port Huron, MI. Alternatively, the slurry used to form the primary coating 122 may be made from conducting carbon powders like acetylene black and/or graphite. For example, one exemplary slurry for the primary coating 122 can be made by mixing commercially available graphite and the binder polyvinyldiflouride (PVDF) in acetone. PVDF can be obtained from Elf Atochem Co. of France, as "Kynar", catalog no. PVDF 2801-00. By way of example, the commercially available graphite may be obtained from Timcal America of Westlake, Ohio, but it should be understood that any other type of graphite may be substituted. Preferably, the amount of conducting carbot powders used in the slurry falls in the range of 25 w% tc 95 w% ("w%" meaning percent by weight), with the remainder of the slurry consisting of the PVDF in acetone. Ideally, the composition of graphite can be between 50 w% and 95 w%.
After the slurry used to form the primary
17 coating 122 is prepared, it is then coated onto the current collector 112 in step 306. Referring to FIG. 5, the slurry is preferably coated onto the aluminum foil current collector 112 with a metering rod 320 to give a wet coating of 125 um. Specifically, the aluminum foil current collector 112 is placed on a granite block 322 that has a smooth surface. The metering rod 320 (such as is available from Diversified Enterprises of Claremont, New Hampshire) includes coils 321. A pipet 324 is used to apply the primary carbon slurry 326 onto the surface of the aluminum foil 112 in front of the metering rod 320. The metering rod 320 is then dragged down the length of the aluminum foil 112 in the direction of arrow 328. The metering rod 320 is kept flush with the aluminum foil 112 while it is being dragged. The carbon slurry will be left in the wake of the metering rod 320 at a thickness dependent on the coil 321 separation distance on the metering rod 320. While use of the metering rod 320 is effective for coating the primary carbon slurry 326 onto the aluminum foil current collector 112, it should be understood that other methods of coating may be used.
In step 308 the coating is air dried for one half hour, and.in step 310 the coating is cured at 80°C
for one hour in an oven. The thickness of the resulting primary coating 122 is about 4 to 6 ~Cm. The resulting primary coated film 312 (i.e., current collector 112 with primary coating 122 thereon) is illustrated in FIG. 6.
The secondary coating 126 is applied on top of the primary coating 122. The secondary coating 126 preferably comprises activated carbon, conducting carbon and a polymer binder. Like the primary coating 122, the secondary coating 126 is also preferably applied in the form of a slurry. The amount of the activated. carbon powder in this slurry preferably falls in the range of 5( to 98 percent-by-weight.
The slurry of activated carbon, conducting
In step 308 the coating is air dried for one half hour, and.in step 310 the coating is cured at 80°C
for one hour in an oven. The thickness of the resulting primary coating 122 is about 4 to 6 ~Cm. The resulting primary coated film 312 (i.e., current collector 112 with primary coating 122 thereon) is illustrated in FIG. 6.
The secondary coating 126 is applied on top of the primary coating 122. The secondary coating 126 preferably comprises activated carbon, conducting carbon and a polymer binder. Like the primary coating 122, the secondary coating 126 is also preferably applied in the form of a slurry. The amount of the activated. carbon powder in this slurry preferably falls in the range of 5( to 98 percent-by-weight.
The slurry of activated carbon, conducting
18 carbon and a polymer binder used to form the secondary coating 126 is prepared in step 314. The slurry preferably includes the following ingredients: a solvent, a binder, and activated carbon powders. By way of example, the amount of solvent may be 80.6 w%, the amount of binder may be 1.63%, and the amount of activated carbon powder may be 17.77%. Exemplary solvents are either water or acetone. Exemplary binders are PVDF, methyl cellulose and EPDM (Ethylene Propylene Diene Monomer). Activated carbon powders may be obtained from Westvaco High Power of Virginia, or from Spectracorp, catalog no. BP-25.
An exemplary process for the preparation of the slurry used to form the secondary coating 126 is as follows. First, the binder is weighed into a 100mL glass jar to which a magnetic stirbar has been added. The solvent, which has been weighed out in a separate bottle, is added to the jar of the binder. The jar is sealed and set on a stirplate for an hour, with intermittent shaking by hand. During this time, the activated carbon powders and the conductive carbon powders are weighed out in a 100mL beaker and set aside. -After the hour, the jar of binder solution is taken off the stirplate, the stirbar is removed, and the weighed carbon powders are carefully added with a small scoop. The jar is placed under an ordinary kitchen mixer and the mixer is turned on to the lowest speed to allow the carbon powders to get wet.
Once the powders are wet, the speed is increased and the jar moved up and down to provide sufficient mixing of the slurry. The jar is then set below the mixer and allowed to mix for 10 minutes. After completion of mixing,~the lid is~placed on the jar and the slurry is shaken vigorously by hand for approximately 30 seconds. The jar is placed on a jar roller apparatus until it is used.
Once the slurry that will be used to form the secondary coating 126 has been prepared, a desired length of the primary coated film 312 (i.e., collector 112 with
An exemplary process for the preparation of the slurry used to form the secondary coating 126 is as follows. First, the binder is weighed into a 100mL glass jar to which a magnetic stirbar has been added. The solvent, which has been weighed out in a separate bottle, is added to the jar of the binder. The jar is sealed and set on a stirplate for an hour, with intermittent shaking by hand. During this time, the activated carbon powders and the conductive carbon powders are weighed out in a 100mL beaker and set aside. -After the hour, the jar of binder solution is taken off the stirplate, the stirbar is removed, and the weighed carbon powders are carefully added with a small scoop. The jar is placed under an ordinary kitchen mixer and the mixer is turned on to the lowest speed to allow the carbon powders to get wet.
Once the powders are wet, the speed is increased and the jar moved up and down to provide sufficient mixing of the slurry. The jar is then set below the mixer and allowed to mix for 10 minutes. After completion of mixing,~the lid is~placed on the jar and the slurry is shaken vigorously by hand for approximately 30 seconds. The jar is placed on a jar roller apparatus until it is used.
Once the slurry that will be used to form the secondary coating 126 has been prepared, a desired length of the primary coated film 312 (i.e., collector 112 with
19 primary coating 122 thereon) is cut in step 316. This cutting step is illustrated in FIG. 7. In step 342 the secondary slurry that was prepared in step 314 is poured onto the desired length of the primary coated film 312.
In step 344 the secondary slurry is applied to the desired length of the primary coated film 312.
Step 344 may be performed using the metering rod 320 and the granite block 322 shown in FIG. 5.
Specifically, the desired length of the primary coated film 312 is placed on the surface of the granite block 322. The pipet 324 is used to apply the secondary slurry onto the surface of the desired length of the primary coated film 312 in front of the metering rod 320. The metering rod 320 is then dragged as described above. It should be understood, however, that use of the metering rod 320 to apply the secondary slurry is not a requirement of the present invention and that other methods may be used.
The resulting primary and secondary coated carbon film 330, which is illustrated in FIG. 8, is then allowed to dry for approximately ZO minutes in step 346.
When it is dry, the carbon film 330 is ready to be made into electrodes.
It should be understood that the above described process 300 may be used to form the electrodes 102, 104 in the capacitors 100 and 200. In order to form the primary and secondary coatings on the reverse side of the current collector 112 (and 108) that are illustrated in FIG. 2, the carbon film 330 is simply turned over and the appropriate steps in the process 300 are repeated on the second surface.
The above-described method of making carbon powder electrodes makes possible EDLC capacitors having time constants z~ on the order of 0.5 seconds.
Furthermore, the method results in~carbon powder electrodes with a lower resistance than electrodes having only a single coat of activated carbon, conducting carbon, and a binder, i.e., electrodes with no primary (or primer) coating as described above.
In order to illustrate this later point, Tables 1 and 2 below show the difference in performance between 5 carbon powder electrodes without and with a primary (or primer) coat. Specifically, several EDLC capacitor cells were made. The capacitor cells were tested using an impedance analyzer and in some cases by constant current.
The electrodes in all of the capacitor cells identified 10 in both Tables 1 and 2 include one coating that consists primarily of activated carbon powder. The specific composition of the slurry used to make the primarily activated carbon powder coating for each cell is shown in the tables. The difference between Tables 1 and 2 is 15 that the electrodes in the capacitor cells identified in Table 1 do not include a primer coating, whereas the electrodes in the capacitor cells identified in Table 2 do include a primer coating.
Cell Slurry Composition usedResistanceCapacitanceRC
ID
for the Primarily Ohm.cmz F/cm2 Activated Carbon Powder Layer RC0604 BP-25 (90 w~), SFG-44 1402 0.011 15.4 I
, Kynar (8.5 w~) (1.5 w$) RC0605 Same as above 627 0.012 7.2 RC0608 BP-25 (90 w~), SFG-44 964 0.007 7.0 (8 w~), Kynar (2 w~) 9 8 Westvaco-CHR-98-55 (90 10.3 0.16 1.7 -O1-O1 w~), Black Pearl (1.5 w~ K nar 8.5 w~
TABLE 1: Without Primer coating Cell Slurry Composition ResistanceCapacitanceRC
ID used for the Primarily Ohm.cm2 F/cm2 Activated Carbon Powder Layer 51291-1 BP-25 (91.4 w~), ICynar4.62 0.09 0.42 (8.6 w~) 51291-2 Same as above 4.08 0.10 0.39 51291-3 Same as above 7.48 0.09 0.65 51291-4 Same as above 4.39 0.09 0.39 '1'AtiL~ G : Wlzn rrimer ~:vaLlng As can be seen from the tables, capacitor cell resistance and time constants are significantly lower for the capacitor cells identified in Table 2, which are the cells that have a primer coating on the electrodes.
In the tables, BP-25 is an exemplary type of activated carbon powder that is available from Spectracorp, SFG-44 is an exemplary type of graphite that is available from Timcal America, Kynar 2801-00 is an exemplary type of binder that is available from Elf Atochem Co., CHR-98-55 is an exemplary type of activated carbon powder that is available from Westvaco High Power, and Black Pearl is an exemplary type of carbon that is available from Cabot.
In a preferred embodiment of the present invention, the binder content in the slurry used to form the coating that is primarily activated carbon powder is lower than is illustrated in Table 2. A preferred value for the binder content is shown in Table 3, which illustrates the measured performance for capacitor cells having carbon powder electrodes that include a primer coating in accordance with the present invention.
Cell Slurry Composition usedArea CapacitanceRC
ID .
for the Primarily ResistanceF/cm2 ' Activated Carbon PowderOhm.cm2 Layer 51291-1 BP-25 (97 w~), Kynar 4.95 0.12 0.59 (3 w~) 51291-2 Same as above 4.30 0.14 0.58 51291-3 Same as above ~ 5.07 0.12 0.62 51291-4 Same as above 3.94 0.12 0.46 '1'AtiL~ a : WlLi1 rrlmerm:c~acimcj Additional packaging and manufacturing techniques that may be used with the present invention are disclosed in United States Provisional Patent Application Number 60/188,331, entitled "HIGH SPEED
MANUFACTURING OF ULTRACAPACITORS", filed March 9, 2000, by inventors C. Farahmandi, Edward Blank, Chenniah Nanjundiah and Brad Emberger, as attorney docket no.
66238, the full disclosure of which is hereby fully incorporated into the present application by reference.
Furthermore, the full disclosure of United States Patent No. 5,907,472 is hereby fully incorporated into the present application by reference.
While the invention herein disclosed has been described by the specific embodiments and applications thereof, numerous modifications and variations could be made thereto by those skilled in the art without departing from the scope of the invention set forth in the claims.
In step 344 the secondary slurry is applied to the desired length of the primary coated film 312.
Step 344 may be performed using the metering rod 320 and the granite block 322 shown in FIG. 5.
Specifically, the desired length of the primary coated film 312 is placed on the surface of the granite block 322. The pipet 324 is used to apply the secondary slurry onto the surface of the desired length of the primary coated film 312 in front of the metering rod 320. The metering rod 320 is then dragged as described above. It should be understood, however, that use of the metering rod 320 to apply the secondary slurry is not a requirement of the present invention and that other methods may be used.
The resulting primary and secondary coated carbon film 330, which is illustrated in FIG. 8, is then allowed to dry for approximately ZO minutes in step 346.
When it is dry, the carbon film 330 is ready to be made into electrodes.
It should be understood that the above described process 300 may be used to form the electrodes 102, 104 in the capacitors 100 and 200. In order to form the primary and secondary coatings on the reverse side of the current collector 112 (and 108) that are illustrated in FIG. 2, the carbon film 330 is simply turned over and the appropriate steps in the process 300 are repeated on the second surface.
The above-described method of making carbon powder electrodes makes possible EDLC capacitors having time constants z~ on the order of 0.5 seconds.
Furthermore, the method results in~carbon powder electrodes with a lower resistance than electrodes having only a single coat of activated carbon, conducting carbon, and a binder, i.e., electrodes with no primary (or primer) coating as described above.
In order to illustrate this later point, Tables 1 and 2 below show the difference in performance between 5 carbon powder electrodes without and with a primary (or primer) coat. Specifically, several EDLC capacitor cells were made. The capacitor cells were tested using an impedance analyzer and in some cases by constant current.
The electrodes in all of the capacitor cells identified 10 in both Tables 1 and 2 include one coating that consists primarily of activated carbon powder. The specific composition of the slurry used to make the primarily activated carbon powder coating for each cell is shown in the tables. The difference between Tables 1 and 2 is 15 that the electrodes in the capacitor cells identified in Table 1 do not include a primer coating, whereas the electrodes in the capacitor cells identified in Table 2 do include a primer coating.
Cell Slurry Composition usedResistanceCapacitanceRC
ID
for the Primarily Ohm.cmz F/cm2 Activated Carbon Powder Layer RC0604 BP-25 (90 w~), SFG-44 1402 0.011 15.4 I
, Kynar (8.5 w~) (1.5 w$) RC0605 Same as above 627 0.012 7.2 RC0608 BP-25 (90 w~), SFG-44 964 0.007 7.0 (8 w~), Kynar (2 w~) 9 8 Westvaco-CHR-98-55 (90 10.3 0.16 1.7 -O1-O1 w~), Black Pearl (1.5 w~ K nar 8.5 w~
TABLE 1: Without Primer coating Cell Slurry Composition ResistanceCapacitanceRC
ID used for the Primarily Ohm.cm2 F/cm2 Activated Carbon Powder Layer 51291-1 BP-25 (91.4 w~), ICynar4.62 0.09 0.42 (8.6 w~) 51291-2 Same as above 4.08 0.10 0.39 51291-3 Same as above 7.48 0.09 0.65 51291-4 Same as above 4.39 0.09 0.39 '1'AtiL~ G : Wlzn rrimer ~:vaLlng As can be seen from the tables, capacitor cell resistance and time constants are significantly lower for the capacitor cells identified in Table 2, which are the cells that have a primer coating on the electrodes.
In the tables, BP-25 is an exemplary type of activated carbon powder that is available from Spectracorp, SFG-44 is an exemplary type of graphite that is available from Timcal America, Kynar 2801-00 is an exemplary type of binder that is available from Elf Atochem Co., CHR-98-55 is an exemplary type of activated carbon powder that is available from Westvaco High Power, and Black Pearl is an exemplary type of carbon that is available from Cabot.
In a preferred embodiment of the present invention, the binder content in the slurry used to form the coating that is primarily activated carbon powder is lower than is illustrated in Table 2. A preferred value for the binder content is shown in Table 3, which illustrates the measured performance for capacitor cells having carbon powder electrodes that include a primer coating in accordance with the present invention.
Cell Slurry Composition usedArea CapacitanceRC
ID .
for the Primarily ResistanceF/cm2 ' Activated Carbon PowderOhm.cm2 Layer 51291-1 BP-25 (97 w~), Kynar 4.95 0.12 0.59 (3 w~) 51291-2 Same as above 4.30 0.14 0.58 51291-3 Same as above ~ 5.07 0.12 0.62 51291-4 Same as above 3.94 0.12 0.46 '1'AtiL~ a : WlLi1 rrlmerm:c~acimcj Additional packaging and manufacturing techniques that may be used with the present invention are disclosed in United States Provisional Patent Application Number 60/188,331, entitled "HIGH SPEED
MANUFACTURING OF ULTRACAPACITORS", filed March 9, 2000, by inventors C. Farahmandi, Edward Blank, Chenniah Nanjundiah and Brad Emberger, as attorney docket no.
66238, the full disclosure of which is hereby fully incorporated into the present application by reference.
Furthermore, the full disclosure of United States Patent No. 5,907,472 is hereby fully incorporated into the present application by reference.
While the invention herein disclosed has been described by the specific embodiments and applications thereof, numerous modifications and variations could be made thereto by those skilled in the art without departing from the scope of the invention set forth in the claims.
Claims
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US09/569,679 US6627252B1 (en) | 2000-05-12 | 2000-05-12 | Electrochemical double layer capacitor having carbon powder electrodes |
US09/569,679 | 2000-05-12 | ||
PCT/US2001/015333 WO2001088934A1 (en) | 2000-05-12 | 2001-05-11 | Electrochemical double layer capacitor having carbon powder electrodes |
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CA2408618A1 true CA2408618A1 (en) | 2001-11-22 |
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CA002408618A Abandoned CA2408618A1 (en) | 2000-05-12 | 2001-05-11 | Electrochemical double layer capacitor having carbon powder electrodes |
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US (2) | US6627252B1 (en) |
EP (1) | EP1314174B1 (en) |
JP (1) | JP2004520703A (en) |
KR (1) | KR100827891B1 (en) |
CN (1) | CN1315140C (en) |
AT (1) | ATE451705T1 (en) |
AU (1) | AU2001259750A1 (en) |
BR (1) | BR0110763A (en) |
CA (1) | CA2408618A1 (en) |
DE (1) | DE60140753D1 (en) |
IL (1) | IL152674A0 (en) |
MX (1) | MXPA02011172A (en) |
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Families Citing this family (83)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8963681B2 (en) | 1997-10-27 | 2015-02-24 | Direct Source International, Llc | Operating control system for electronic equipment |
CN1236519C (en) * | 2001-04-27 | 2006-01-11 | 钟纺株式会社 | Organic electrolyte battery |
AU2003284179A1 (en) * | 2002-10-25 | 2004-05-13 | Inventqjaya Sdn Bhd | Fluid deionization system |
WO2004077467A1 (en) * | 2003-02-25 | 2004-09-10 | Zeon Corporation | Process for producing electrode for electrochemical device |
US7791860B2 (en) | 2003-07-09 | 2010-09-07 | Maxwell Technologies, Inc. | Particle based electrodes and methods of making same |
US7508651B2 (en) * | 2003-07-09 | 2009-03-24 | Maxwell Technologies, Inc. | Dry particle based adhesive and dry film and methods of making same |
US20060147712A1 (en) * | 2003-07-09 | 2006-07-06 | Maxwell Technologies, Inc. | Dry particle based adhesive electrode and methods of making same |
US7352558B2 (en) | 2003-07-09 | 2008-04-01 | Maxwell Technologies, Inc. | Dry particle based capacitor and methods of making same |
US7342770B2 (en) * | 2003-07-09 | 2008-03-11 | Maxwell Technologies, Inc. | Recyclable dry particle based adhesive electrode and methods of making same |
US7295423B1 (en) | 2003-07-09 | 2007-11-13 | Maxwell Technologies, Inc. | Dry particle based adhesive electrode and methods of making same |
US7920371B2 (en) * | 2003-09-12 | 2011-04-05 | Maxwell Technologies, Inc. | Electrical energy storage devices with separator between electrodes and methods for fabricating the devices |
DE10347568A1 (en) | 2003-10-14 | 2005-05-12 | Degussa | Capacitor with ceramic separation layer |
US7495349B2 (en) | 2003-10-20 | 2009-02-24 | Maxwell Technologies, Inc. | Self aligning electrode |
JP2005191423A (en) * | 2003-12-26 | 2005-07-14 | Tdk Corp | Electrode for capacitor |
JP2005191425A (en) * | 2003-12-26 | 2005-07-14 | Tdk Corp | Production process of electrode for capacitor |
JP4720999B2 (en) * | 2004-02-16 | 2011-07-13 | 日本電気株式会社 | Power storage device |
JP4721000B2 (en) * | 2004-02-16 | 2011-07-13 | 日本電気株式会社 | Power storage device |
US7090946B2 (en) | 2004-02-19 | 2006-08-15 | Maxwell Technologies, Inc. | Composite electrode and method for fabricating same |
US7384433B2 (en) | 2004-02-19 | 2008-06-10 | Maxwell Technologies, Inc. | Densification of compressible layers during electrode lamination |
US7419745B2 (en) * | 2004-03-31 | 2008-09-02 | Sanjay Chaturvedi | Method of forming an electrode structure useful in energy storage devices |
US7227737B2 (en) | 2004-04-02 | 2007-06-05 | Maxwell Technologies, Inc. | Electrode design |
US7489517B2 (en) * | 2004-04-05 | 2009-02-10 | Thomas Joel Massingill | Die down semiconductor package |
EP1624472A3 (en) * | 2004-07-08 | 2011-03-16 | Sumitomo Chemical Company, Limited | Porous Electrodes, Devices including the Porous Electrodes, and Methods for their Production |
US7245478B2 (en) | 2004-08-16 | 2007-07-17 | Maxwell Technologies, Inc. | Enhanced breakdown voltage electrode |
US8057567B2 (en) | 2004-11-05 | 2011-11-15 | Donaldson Company, Inc. | Filter medium and breather filter structure |
PL2308579T3 (en) | 2004-11-05 | 2016-06-30 | Donaldson Co Inc | Aerosol separator |
US7400490B2 (en) * | 2005-01-25 | 2008-07-15 | Naturalnano Research, Inc. | Ultracapacitors comprised of mineral microtubules |
KR100672599B1 (en) | 2005-01-26 | 2007-01-24 | 엘지전자 주식회사 | Energy storage capacitor and method for fabricating the same |
KR100672310B1 (en) | 2005-02-04 | 2007-01-24 | 엘지전자 주식회사 | Energy storage capacitor and method for fabricating the same |
US8663845B2 (en) * | 2005-02-10 | 2014-03-04 | Showa Denko K.K. | Secondary-battery current collector, secondary-battery cathode, secondary-battery anode, secondary battery and production method thereof |
US7440258B2 (en) | 2005-03-14 | 2008-10-21 | Maxwell Technologies, Inc. | Thermal interconnects for coupling energy storage devices |
US7511941B1 (en) * | 2005-06-08 | 2009-03-31 | Maxwell Technologies, Inc. | Ultrasonic sealed fill hole |
US8313723B2 (en) * | 2005-08-25 | 2012-11-20 | Nanocarbons Llc | Activated carbon fibers, methods of their preparation, and devices comprising activated carbon fibers |
WO2007043515A1 (en) | 2005-10-11 | 2007-04-19 | Showa Denko K.K. | Electric double layer capacitor |
CN101313376A (en) * | 2005-11-22 | 2008-11-26 | 麦斯韦尔技术股份有限公司 | Ultracapacitor electrode with controlled carbon content |
US7692411B2 (en) * | 2006-01-05 | 2010-04-06 | Tpl, Inc. | System for energy harvesting and/or generation, storage, and delivery |
US20070178310A1 (en) | 2006-01-31 | 2007-08-02 | Rudyard Istvan | Non-woven fibrous materials and electrodes therefrom |
AU2007239058A1 (en) * | 2006-02-15 | 2007-10-25 | Rudyard Lyle Istvan | Mesoporous activated carbons |
JP4878881B2 (en) * | 2006-03-17 | 2012-02-15 | 日本ゴア株式会社 | Electrode for electric double layer capacitor and electric double layer capacitor |
US7864507B2 (en) | 2006-09-06 | 2011-01-04 | Tpl, Inc. | Capacitors with low equivalent series resistance |
US8518573B2 (en) | 2006-09-29 | 2013-08-27 | Maxwell Technologies, Inc. | Low-inductive impedance, thermally decoupled, radii-modulated electrode core |
WO2008049037A2 (en) * | 2006-10-17 | 2008-04-24 | Maxwell Technologies, Inc. | Electrode for energy storage device |
US20080151472A1 (en) * | 2006-12-20 | 2008-06-26 | Maletin Yuriy A | Electrochemical double layer capacitor |
US20080165470A1 (en) * | 2007-01-09 | 2008-07-10 | Korea Electronics Technology Institute | Functional Carbon Material and Method of Producing the Same |
KR20100110719A (en) | 2007-02-14 | 2010-10-13 | 유니버시티 오브 켄터키 리서치 파운데이션 | Methods of forming activated carbons |
US20080204973A1 (en) * | 2007-02-28 | 2008-08-28 | Maxwell Technologies, Inc. | Ultracapacitor electrode with controlled iron content |
US20080201925A1 (en) | 2007-02-28 | 2008-08-28 | Maxwell Technologies, Inc. | Ultracapacitor electrode with controlled sulfur content |
US20080274407A1 (en) * | 2007-05-03 | 2008-11-06 | Roy Joseph Bourcier | Layered carbon electrodes for capacitive deionization and methods of making the same |
US20080297980A1 (en) * | 2007-05-31 | 2008-12-04 | Roy Joseph Bourcier | Layered carbon electrodes useful in electric double layer capacitors and capacitive deionization and methods of making the same |
US8159312B2 (en) | 2007-06-27 | 2012-04-17 | Medrelief Inc. | Method and system for signal coupling and direct current blocking |
CN101140828B (en) * | 2007-09-12 | 2010-06-23 | 浙江大学宁波理工学院 | Technique for large-scale producing super capacitor |
WO2009152239A1 (en) * | 2008-06-10 | 2009-12-17 | Nanotune Technologies Corp. | Nanoporous electrodes and related devices and methods |
US8178241B2 (en) * | 2008-08-28 | 2012-05-15 | 3M Innovative Properties Company | Electrode including current collector with nano-scale coating and method of making the same |
DE102008062765A1 (en) | 2008-12-18 | 2010-07-01 | Vb Autobatterie Gmbh & Co. Kgaa | Textile sheet material for a battery electrode |
JP2012519357A (en) | 2009-02-26 | 2012-08-23 | ジョンソン コントロールズ テクノロジー カンパニー | Battery electrode and manufacturing method thereof |
EP2462598A1 (en) | 2009-07-27 | 2012-06-13 | The Paper Battery Co. | Compliant energy storing structural sheet |
KR20110035906A (en) * | 2009-09-30 | 2011-04-06 | 가부시키가이샤 한도오따이 에네루기 켄큐쇼 | Capacitor |
PL2497137T3 (en) | 2009-11-02 | 2020-03-31 | Cabot Corporation | Lead-acid batteries and pastes therefor |
WO2011053668A1 (en) | 2009-11-02 | 2011-05-05 | Cabot Corporation | High surface area and low structure carbon blacks for energy storage applications |
CN101710537B (en) * | 2009-12-09 | 2011-05-11 | 上海奥威科技开发有限公司 | Electrode for super capacitor and manufacturing method thereof |
US7931985B1 (en) * | 2010-11-08 | 2011-04-26 | International Battery, Inc. | Water soluble polymer binder for lithium ion battery |
US8076026B2 (en) * | 2010-02-05 | 2011-12-13 | International Battery, Inc. | Rechargeable battery using an aqueous binder |
KR101079497B1 (en) * | 2010-02-16 | 2011-11-03 | 삼성전기주식회사 | Methods for manufacturing electric double layer capacitor cell and electric double layer capacitor and apparatus for manufacturing electric double layer capacitor cell |
CN101894682B (en) * | 2010-02-26 | 2012-07-04 | 上海奥威科技开发有限公司 | High-energy ultracapacitor |
CN101847514B (en) * | 2010-03-23 | 2015-10-14 | 集盛星泰(北京)科技有限公司 | A kind of activated carbon electrodes and there is the ultracapacitor of this electrode |
CN101923962B (en) * | 2010-03-23 | 2015-09-23 | 集盛星泰(北京)科技有限公司 | A kind of active carbon electrode and the ultracapacitor comprising this electrode |
EE201000051A (en) * | 2010-06-04 | 2012-02-15 | OÜ@Skeleton@Technologies | High t "" multi-element supercapacitor |
US20110143206A1 (en) * | 2010-07-14 | 2011-06-16 | International Battery, Inc. | Electrode for rechargeable batteries using aqueous binder solution for li-ion batteries |
US8102642B2 (en) * | 2010-08-06 | 2012-01-24 | International Battery, Inc. | Large format ultracapacitors and method of assembly |
CN102332354B (en) * | 2010-12-31 | 2013-06-05 | 东莞新能源科技有限公司 | Super capacitor, pole piece thereof and pole piece fabrication method |
EP2689438B1 (en) | 2011-03-23 | 2022-11-16 | Mespilus Inc. | Polarized electrode for flow-through capacitive deionization |
WO2012138315A1 (en) * | 2011-04-07 | 2012-10-11 | Lithdyne, LLC | Carbon electrodes and electrochemical capacitors |
CN102543484A (en) * | 2012-03-28 | 2012-07-04 | 长沙海密特新能源科技有限公司 | High-power flexible package supercapacitor pole piece and production method thereof |
EP2962996B8 (en) * | 2014-07-02 | 2020-12-30 | Voltea Limited | Method to prepare a coated current collector electrode for a flow through capacitor using two solvents with different boiling points |
CN104282443A (en) * | 2014-09-18 | 2015-01-14 | 鸿源控股有限公司 | Flat-plate-type super capacitor |
CN106033816B (en) * | 2014-12-11 | 2019-02-12 | 日本蓄电器工业株式会社 | The electrode manufacturing method using three-dimensional shape electrode matrix of electrochemical applications product |
EP3248394A4 (en) | 2015-01-19 | 2018-09-12 | 3M Innovative Properties Company | Hearing protection device with convoluted acoustic horn |
CN109196612A (en) | 2016-05-20 | 2019-01-11 | 阿维科斯公司 | The supercapacitor used at high temperature |
CN115512980A (en) | 2016-05-20 | 2022-12-23 | 京瓷Avx元器件公司 | Nonaqueous electrolyte for super capacitor |
KR20190003793A (en) | 2016-05-20 | 2019-01-09 | 에이브이엑스 코포레이션 | Electrode Structure for Ultra Capacitor |
WO2018140367A1 (en) | 2017-01-27 | 2018-08-02 | Cabot Corporation | Supercapacitors containing carbon black particles cleaned with an acid |
CN109545564B (en) * | 2018-11-26 | 2021-05-04 | 韶关东阳光包装印刷有限公司 | Carbon-coated aluminum foil for solid aluminum capacitor and preparation method thereof |
EP4062467A1 (en) | 2019-11-21 | 2022-09-28 | Volkswagen Aktiengesellschaft | Dry electrode manufacturing |
Family Cites Families (138)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA849697A (en) | 1970-08-18 | General Electric Company | Capacitor with ionic conducting ceramic electrolyte | |
US2234608A (en) | 1934-11-24 | 1941-03-11 | Sprague Specialties Co | Electrolytic device and the manufacture of same |
US3288641A (en) | 1962-06-07 | 1966-11-29 | Standard Oil Co | Electrical energy storage apparatus |
US3536963A (en) | 1968-05-29 | 1970-10-27 | Standard Oil Co | Electrolytic capacitor having carbon paste electrodes |
US3617387A (en) | 1969-02-20 | 1971-11-02 | Union Carbide Corp | Battery construction having cell components completely internally bonded with adhesive |
CA980038A (en) | 1969-04-23 | 1975-12-16 | Dexter Worden | Flexible, non-woven compositions and process for producing same |
SE392582B (en) | 1970-05-21 | 1977-04-04 | Gore & Ass | PROCEDURE FOR THE PREPARATION OF A POROST MATERIAL, BY EXPANDING AND STRETCHING A TETRAFLUORETENE POLYMER PREPARED IN AN PASTE-FORMING EXTENSION PROCEDURE |
US3648337A (en) | 1970-08-24 | 1972-03-14 | Mallory & Co Inc P R | Encapsulating of electronic components |
US3838092A (en) | 1971-04-21 | 1974-09-24 | Kewanee Oil Co | Dustless compositions containing fiberous polytetrafluoroethylene |
US3935029A (en) | 1971-11-18 | 1976-01-27 | Energy Research Corporation | Method of fabricating a carbon - polytetrafluoroethylene electrode - support |
US3977901A (en) | 1974-10-23 | 1976-08-31 | Westinghouse Electric Corporation | Metal/air cells and improved air electrodes for use therein |
US4005222A (en) | 1975-05-21 | 1977-01-25 | Mead Johnson & Company | Mucolytic mercaptoacylamidobenzoic and benzenesulfonic acid compounds and process |
CA1088149A (en) | 1976-06-15 | 1980-10-21 | Gerda M. Kohlmayr | Method of fabricating a fuel cell electrode |
US4086397A (en) | 1977-01-31 | 1978-04-25 | Gte Laboratories Incorporated | Electrochemical cell and cathode for same |
US4153661A (en) | 1977-08-25 | 1979-05-08 | Minnesota Mining And Manufacturing Company | Method of making polytetrafluoroethylene composite sheet |
US4278525A (en) | 1978-04-24 | 1981-07-14 | Diamond Shamrock Corporation | Oxygen cathode for alkali-halide electrolysis cell |
US4327400A (en) | 1979-01-10 | 1982-04-27 | Matsushita Electric Industrial Co., Ltd. | Electric double layer capacitor |
FR2468218A1 (en) | 1979-10-18 | 1981-04-30 | Alsthom Cgee | METHOD OF MANUFACTURING BY CALENDERING POROUS THIN STRIPS AND PRODUCTS OBTAINED, ESPECIALLY ELECTRODES FOR FUEL CELLS |
JPS6013292B2 (en) * | 1979-11-08 | 1985-04-06 | マルコン電子株式会社 | electric double layer capacitor |
US4341847A (en) | 1980-10-14 | 1982-07-27 | Institute Of Gas Technology | Electrochemical zinc-oxygen cell |
US4354958A (en) | 1980-10-31 | 1982-10-19 | Diamond Shamrock Corporation | Fibrillated matrix active layer for an electrode |
US4337140A (en) | 1980-10-31 | 1982-06-29 | Diamond Shamrock Corporation | Strengthening of carbon black-teflon-containing electrodes |
US4500647A (en) | 1980-10-31 | 1985-02-19 | Diamond Shamrock Chemicals Company | Three layer laminated matrix electrode |
US4379772A (en) | 1980-10-31 | 1983-04-12 | Diamond Shamrock Corporation | Method for forming an electrode active layer or sheet |
US4320185A (en) | 1981-01-19 | 1982-03-16 | Mpd Technology Corporation | Production of a cell electrode system |
US4396693A (en) | 1981-01-19 | 1983-08-02 | Mpd Technology Corporation | Production of a cell electrode system |
US4320184A (en) | 1981-01-19 | 1982-03-16 | Mpd Technology Corporation | Production of a cell electrode system |
EP0063981B1 (en) | 1981-04-13 | 1987-11-11 | Societe Les Piles Wonder | Method of manufacturing thin electrodes, particularly gas electrodes, for electrochemical devices, and thin electrodes obtained by such a method, the electrodes possibly being provided with current collectors |
US4457953A (en) | 1981-12-23 | 1984-07-03 | The Dow Chemical Company | Electrode material |
US4562511A (en) * | 1982-06-30 | 1985-12-31 | Matsushita Electric Industrial Co., Ltd. | Electric double layer capacitor |
JPS603120A (en) | 1983-06-21 | 1985-01-09 | 株式会社村田製作所 | Method of producing electric double layer capacitor |
US4597028A (en) * | 1983-08-08 | 1986-06-24 | Matsushita Electric Industrial Co., Ltd. | Electric double layer capacitor and method for producing the same |
US4556618A (en) | 1983-12-01 | 1985-12-03 | Allied Corporation | Battery electrode and method of making |
JPS60181289A (en) | 1984-02-27 | 1985-09-14 | Japan Goatetsukusu Kk | Material for gas diffusible electrode |
US4664683A (en) | 1984-04-25 | 1987-05-12 | Pall Corporation | Self-supporting structures containing immobilized carbon particles and method for forming same |
WO1986000750A1 (en) | 1984-07-17 | 1986-01-30 | Matsushita Electric Industrial Co., Ltd. | Polarizable electrode and production method thereof |
FR2577165B1 (en) | 1985-02-12 | 1987-08-21 | Conceptions Innovations Atel | PROCESS FOR THE PREPARATION AND RENOVATION OF A MELTING ROLL FOR A XEROGRAPHIC MACHINE, MELTING ROLL AND VULCANIZABLE COMPOSITION |
JPH07105316B2 (en) | 1985-08-13 | 1995-11-13 | 旭硝子株式会社 | Polarizable electrode for electric double layer capacitor and method for manufacturing the same |
US4853305A (en) | 1986-03-24 | 1989-08-01 | W. R. Grace & Co.-Conn. | Cathodic electrode |
JPH078532B2 (en) | 1986-05-30 | 1995-02-01 | 三菱油化株式会社 | Drawing method for resin sheet |
US4730239A (en) | 1986-10-29 | 1988-03-08 | Stemcor Corporation | Double layer capacitors with polymeric electrolyte |
JPS63268221A (en) | 1987-04-27 | 1988-11-04 | Matsushita Electric Ind Co Ltd | Electric double-layer capacitor |
US4760494A (en) | 1987-07-22 | 1988-07-26 | General Electric Company | Capacitor containing an adsorbent material |
JPS6446913A (en) | 1987-08-17 | 1989-02-21 | Kanebo Ltd | Electric double layer capacitor |
CA1309134C (en) | 1987-09-25 | 1992-10-20 | Wilfrid B. O'callaghan | Metal/air battery with recirculating electrolyte |
US4804592A (en) | 1987-10-16 | 1989-02-14 | The United States Of America As Represented By The United States Department Of Energy | Composite electrode for use in electrochemical cells |
JPH01222425A (en) | 1988-03-01 | 1989-09-05 | Asahi Glass Co Ltd | Electric double layer capacitor |
JPH01246812A (en) | 1988-03-29 | 1989-10-02 | Asahi Glass Co Ltd | Electric double-layer capacitor |
US5019311A (en) | 1989-02-23 | 1991-05-28 | Koslow Technologies Corporation | Process for the production of materials characterized by a continuous web matrix or force point bonding |
US5277729A (en) | 1989-03-08 | 1994-01-11 | Murata Manufacturing Co., Ltd. | Method of manufacturing polarizable electrode for electric double-layer capacitor |
US4985296A (en) | 1989-03-16 | 1991-01-15 | W. L. Gore & Associates, Inc. | Polytetrafluoroethylene film |
JPH065658B2 (en) | 1989-07-29 | 1994-01-19 | いすゞ自動車株式会社 | Arrangement structure of electric double layer capacitor cell |
JPH0666235B2 (en) | 1989-09-02 | 1994-08-24 | いすゞ自動車株式会社 | Electric double layer capacitor |
JPH0748464B2 (en) | 1989-09-12 | 1995-05-24 | いすゞ自動車株式会社 | Electric double layer capacitor |
JPH067539B2 (en) | 1989-09-14 | 1994-01-26 | いすゞ自動車株式会社 | Electric double layer capacitor |
JPH0666230B2 (en) | 1990-01-30 | 1994-08-24 | いすゞ自動車株式会社 | Electric double layer capacitor |
JP2840780B2 (en) | 1990-02-20 | 1998-12-24 | 富士電気化学株式会社 | Electric double layer capacitor |
US5071610A (en) | 1990-02-23 | 1991-12-10 | Minnesota Mining And Manufacturing Company | Method of making a controlled pore composite polytetrafluoroethylene |
US5147539A (en) | 1990-02-23 | 1992-09-15 | Minnesota Mining And Manufacturing Company | Controlled pore composite polytetrafluoroethylene article |
US5172307A (en) | 1990-03-23 | 1992-12-15 | Nec Corporation | Activated carbon/polyacene composite and process for producing the same |
DE69128805T2 (en) * | 1990-03-29 | 1998-05-14 | Matsushita Electric Ind Co Ltd | Electrolytic double layer capacitor and process for its manufacture |
JP2690187B2 (en) * | 1990-10-25 | 1997-12-10 | 松下電器産業株式会社 | Electric double layer capacitor |
US5620597A (en) | 1990-04-23 | 1997-04-15 | Andelman; Marc D. | Non-fouling flow-through capacitor |
DE4015363A1 (en) | 1990-05-12 | 1991-11-14 | Varta Batterie | METHOD FOR PRODUCING A POSITIVE ELECTRODE IN TAPE FOR PRIMARY AND SECONDARY ELEMENTS, AND A DEVICE FOR THIS METHOD |
JP3132009B2 (en) | 1990-12-28 | 2001-02-05 | 武田薬品工業株式会社 | Water-soluble oligomer and method for producing the same |
US5145752A (en) | 1990-12-31 | 1992-09-08 | Luz Electric Fuel Israel Limited | Electrodes for metal/air batteries and bipolar metal/air batteries incorporating the same |
US5190833A (en) | 1990-12-31 | 1993-03-02 | Luz Electric Fuel Israel Ltd. | Electrodes for metal/air batteries and fuel cells and bipolar metal/air batteries incorporating the same |
JPH04274311A (en) | 1991-03-01 | 1992-09-30 | Nec Corp | Electrical double-layer capacitor |
DE4141416A1 (en) | 1991-12-11 | 1993-06-17 | Schering Ag | METHOD FOR COATING SURFACES WITH FINE-PARTICLE SOLID PARTICLES |
JPH05121274A (en) | 1991-09-05 | 1993-05-18 | Rohm Co Ltd | Solid electrolytic capacitor and its manufacture |
US5351164A (en) | 1991-10-29 | 1994-09-27 | T.N. Frantsevich Institute For Problems In Materials Science | Electrolytic double layer capacitor |
FR2685122B1 (en) | 1991-12-13 | 1994-03-25 | Alcatel Alsthom Cie Gle Electric | CONDUCTIVE POLYMER-BASED SUPERCAPACITOR. |
US5381303A (en) * | 1992-05-20 | 1995-01-10 | Matsushita Electric Industrial Co., Ltd. | Electric double layer capacitor and method for manufacture thereof |
JPH0677089A (en) | 1992-05-27 | 1994-03-18 | Nec Corp | Electric double-layer capacitor |
US5350643A (en) | 1992-06-02 | 1994-09-27 | Hitachi, Ltd. | Solid polymer electrolyte type fuel cell |
US5665212A (en) | 1992-09-04 | 1997-09-09 | Unisearch Limited Acn 000 263 025 | Flexible, conducting plastic electrode and process for its preparation |
US5917693A (en) | 1992-10-26 | 1999-06-29 | Dai-Ichi Kogyo Seiyaku Co., Ltd. | Electrically conductive polymer composition |
US5697390A (en) | 1993-01-29 | 1997-12-16 | Coltec Industries Inc | Process for producing filled polytetrafluoroethylene resin composite materials and products |
RU2099807C1 (en) | 1993-02-16 | 1997-12-20 | Акционерное общество "Элит" | Capacitor with double electric layer |
DE4313474C2 (en) | 1993-04-24 | 1997-02-13 | Dornier Gmbh | Double layer capacitor, which is composed of double layer capacitor units and its use as an electrochemical energy store |
US5381301A (en) | 1993-05-11 | 1995-01-10 | Aerovox Incorporated | Leak-tight and rupture proof, ultrasonically-welded, polymer-encased electrical capacitor with pressure sensitive circuit interrupter |
US5581438A (en) | 1993-05-21 | 1996-12-03 | Halliop; Wojtek | Supercapacitor having electrodes with non-activated carbon fibers |
JP3335218B2 (en) | 1993-05-24 | 2002-10-15 | 日清紡績株式会社 | Glassy carbon-activated carbon composite material, method for producing the same, and polarizable electrode for electric double layer capacitor using the glassy carbon-activated carbon composite material |
US5318862A (en) | 1993-09-22 | 1994-06-07 | Westinghouse Electric Corp. | Bifunctional gas diffusion electrodes employing wettable, non-wettable layered structure using the mud-caking concept |
US5748438A (en) | 1993-10-04 | 1998-05-05 | Motorola, Inc. | Electrical energy storage device having a porous organic electrode |
JPH07106206A (en) | 1993-10-06 | 1995-04-21 | Nec Corp | Electric double layer capacitor |
US5393617A (en) | 1993-10-08 | 1995-02-28 | Electro Energy, Inc. | Bipolar electrochmeical battery of stacked wafer cells |
FR2712733B1 (en) | 1993-11-16 | 1996-02-09 | Bollore Technologies | Method of manufacturing a multilayer electrochemical assembly comprising an electrolyte between two electrodes and assembly thus produced. |
JPH07161589A (en) | 1993-12-06 | 1995-06-23 | Nisshinbo Ind Inc | Electric double-layer capacitor |
US5468574A (en) | 1994-05-23 | 1995-11-21 | Dais Corporation | Fuel cell incorporating novel ion-conducting membrane |
KR100366551B1 (en) | 1994-09-29 | 2003-03-12 | 닛뽄 케미콘 가부시끼가이샤 | Electrolytic Capacitors |
US5585999A (en) | 1994-09-30 | 1996-12-17 | The United States Of America As Represented By The Secretary Of The Air Force | Supercapacitor electrochemical cell |
US5621607A (en) * | 1994-10-07 | 1997-04-15 | Maxwell Laboratories, Inc. | High performance double layer capacitors including aluminum carbon composite electrodes |
US5862035A (en) * | 1994-10-07 | 1999-01-19 | Maxwell Energy Products, Inc. | Multi-electrode double layer capacitor having single electrolyte seal and aluminum-impregnated carbon cloth electrodes |
JP3446339B2 (en) | 1994-10-18 | 2003-09-16 | 三菱化学株式会社 | Activated carbon production method |
JPH08138978A (en) | 1994-11-02 | 1996-05-31 | Japan Gore Tex Inc | Electric double layer capacitor and manufacture of its electrode |
JPH08143771A (en) | 1994-11-25 | 1996-06-04 | Nec Corp | Heat-resistant poltaniline, derivative therefrom, solid electrolytic capacitor, and process for producing the same |
EP0714108B1 (en) | 1994-11-25 | 1999-11-03 | Nec Corporation | Solid electrolytic capacitor having two solid electrolyte layers and method of manufacturing the same |
US5659457A (en) | 1995-04-07 | 1997-08-19 | Motorola, Inc. | Carbon electrodes and energy storage device made thereof |
AU5541996A (en) * | 1995-04-12 | 1996-10-30 | Valence Technology, Inc. | Curable alkane multifunctional acrylates based solid electro lytes and electrolytic cells produced therefrom |
US5748439A (en) | 1995-06-06 | 1998-05-05 | Telectronics Pacing Systems, Inc. | Capacitors having high strength electrolytic capacitor separators |
US5751541A (en) * | 1995-07-05 | 1998-05-12 | Motorola, Inc. | Polymer electrodes for energy storage devices and method of making same |
JP3252705B2 (en) | 1995-07-17 | 2002-02-04 | トヨタ自動車株式会社 | Electric double layer capacitor |
US5620807A (en) | 1995-08-31 | 1997-04-15 | The Dow Chemical Company | Flow field assembly for electrochemical fuel cells |
US5926361A (en) | 1995-09-28 | 1999-07-20 | Westvaco Corporation | High power density double layer energy storage devices |
AU1116397A (en) | 1995-10-31 | 1997-05-22 | Tjt Technologies, Inc. | High surface area mesoporous desigel materials and methods for their fabrication |
JP3028056B2 (en) | 1996-02-19 | 2000-04-04 | 日本電気株式会社 | Electric double layer capacitor basic cell and electric double layer capacitor |
US5812367A (en) | 1996-04-04 | 1998-09-22 | Matsushita Electric Industrial Co., Ltd. | Solid electrolytic capacitors comprising a conductive layer made of a polymer of pyrrole or its derivative |
KR100442073B1 (en) | 1996-04-26 | 2004-09-18 | 닛뽄 케미콘 가부시끼가이샤 | Solid Electrolyte Capacitor and its Manufacture |
DE19629154C2 (en) | 1996-07-19 | 2000-07-06 | Dornier Gmbh | Bipolar electrode-electrolyte unit |
DE19704584C2 (en) | 1997-02-07 | 1999-02-25 | Dornier Gmbh | Double-layer capacitor consisting of several double-layer capacitor single cells, usable as energy storage, current source or electronic component |
US5850331A (en) | 1996-08-30 | 1998-12-15 | Honda Giken Kogyo Kabushiki Kaisha | Electric double-layer capacitor and capacitor device |
JPH10144571A (en) | 1996-09-13 | 1998-05-29 | Tdk Corp | Solid electric double layer capacitor |
US5877935A (en) | 1996-09-17 | 1999-03-02 | Honda Giken Kogyo Kabushiki-Kaisha | Active carbon used for electrode for organic solvent type electric double layer capacitor |
US5793603A (en) | 1996-11-19 | 1998-08-11 | Boundless Corp. | Ultracapacitor design having a honey comb structure |
US5875092A (en) | 1997-02-07 | 1999-02-23 | The United States Of America As Represented By The Secretary Of The Army | Proton inserted ruthenium oxide electrode material for electrochemical capacitors |
JPH10275747A (en) * | 1997-03-28 | 1998-10-13 | Nec Corp | Electric double layer capacitor |
US5920455A (en) | 1997-05-01 | 1999-07-06 | Wilson Greatbatch Ltd. | One step ultrasonically coated substrate for use in a capacitor |
US5949638A (en) | 1997-05-02 | 1999-09-07 | Cm Components, Inc. | Multiple anode capacitor |
JP3201516B2 (en) | 1997-07-18 | 2001-08-20 | ユーエイチティー株式会社 | Perforator |
JPH11102844A (en) * | 1997-07-28 | 1999-04-13 | Matsushita Electric Ind Co Ltd | Electrical double layer capacitor and manufacture thereof |
US6127474A (en) | 1997-08-27 | 2000-10-03 | Andelman; Marc D. | Strengthened conductive polymer stabilized electrode composition and method of preparing |
JPH1177787A (en) | 1997-09-02 | 1999-03-23 | Daikin Ind Ltd | Production of highly conductive polytetrafluoroethylene sheet and highly conductive polytetrafluoroethylene wide and long sheet |
US6134760A (en) | 1997-09-22 | 2000-10-24 | Mushiake; Naofumi | Process for manufacturing electric double layer capacitor |
JP4968977B2 (en) * | 1997-09-22 | 2012-07-04 | 日本ゴア株式会社 | Polarized electrode body and manufacturing method thereof |
US5847920A (en) | 1997-09-25 | 1998-12-08 | Motorola, Inc. | Electrochemical capacitor with hybrid polymer polyacid electrolyte |
US6383427B2 (en) | 1997-12-24 | 2002-05-07 | Asahi Glass Company, Ltd. | Process for producing an electric double layer capacitor electrode |
US6195251B1 (en) | 1997-10-29 | 2001-02-27 | Asahi Glass Company Ltd. | Electrode assembly and electric double layer capacitor having the electrode assembly |
DE69834706T2 (en) | 1997-12-22 | 2007-06-06 | Asahi Glass Co., Ltd. | Electric double layer capacitor |
US6493210B2 (en) | 1998-01-23 | 2002-12-10 | Matsushita Electric Industrial Co., Ltd. | Electrode metal material, capacitor and battery formed of the material and method of producing the material and the capacitor and battery |
WO1999038177A1 (en) * | 1998-01-23 | 1999-07-29 | Matsushita Electric Industrial Co., Ltd. | Metal electrode material, capacitor using metal electrode material, and method of manufacture |
US6127060A (en) | 1998-06-17 | 2000-10-03 | Aer Energy Resources, Inc. | Recharge catalyst with thin film low corrosion coating, metal-air electrode including said catalyst and methods for making said catalyst and electrode |
JP2000049055A (en) | 1998-07-27 | 2000-02-18 | Asahi Glass Co Ltd | Electric double layer capacitor and electrode for it |
US6072692A (en) | 1998-10-08 | 2000-06-06 | Asahi Glass Company, Ltd. | Electric double layer capacitor having an electrode bonded to a current collector via a carbon type conductive adhesive layer |
JP2000315632A (en) | 1999-03-02 | 2000-11-14 | Matsushita Electric Ind Co Ltd | Capacitor |
US6456484B1 (en) | 1999-08-23 | 2002-09-24 | Honda Giken Kogyo Kabushiki Kaisha | Electric double layer capacitor |
EP1096521A3 (en) | 1999-10-27 | 2001-11-21 | Asahi Glass Co., Ltd. | Electric double layer capacitor |
US6368365B1 (en) | 2000-03-23 | 2002-04-09 | The Gillette Company | Method of making a battery |
-
2000
- 2000-05-12 US US09/569,679 patent/US6627252B1/en not_active Expired - Lifetime
-
2001
- 2001-05-11 WO PCT/US2001/015333 patent/WO2001088934A1/en active Application Filing
- 2001-05-11 AU AU2001259750A patent/AU2001259750A1/en not_active Abandoned
- 2001-05-11 BR BR0110763-1A patent/BR0110763A/en not_active Application Discontinuation
- 2001-05-11 CN CNB018127665A patent/CN1315140C/en not_active Expired - Lifetime
- 2001-05-11 RU RU2002133444/09A patent/RU2002133444A/en not_active Application Discontinuation
- 2001-05-11 JP JP2001584441A patent/JP2004520703A/en active Pending
- 2001-05-11 CA CA002408618A patent/CA2408618A1/en not_active Abandoned
- 2001-05-11 AT AT01933318T patent/ATE451705T1/en not_active IP Right Cessation
- 2001-05-11 EP EP01933318A patent/EP1314174B1/en not_active Expired - Lifetime
- 2001-05-11 KR KR1020027015201A patent/KR100827891B1/en active IP Right Grant
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KR100827891B1 (en) | 2008-05-07 |
US20040085709A1 (en) | 2004-05-06 |
US6804108B2 (en) | 2004-10-12 |
US6627252B1 (en) | 2003-09-30 |
CN1483210A (en) | 2004-03-17 |
CN1315140C (en) | 2007-05-09 |
WO2001088934A1 (en) | 2001-11-22 |
RU2002133444A (en) | 2004-04-20 |
EP1314174B1 (en) | 2009-12-09 |
AU2001259750A1 (en) | 2001-11-26 |
EP1314174A4 (en) | 2005-08-03 |
ATE451705T1 (en) | 2009-12-15 |
BR0110763A (en) | 2003-05-06 |
MXPA02011172A (en) | 2004-09-09 |
IL152674A0 (en) | 2003-06-24 |
EP1314174A1 (en) | 2003-05-28 |
JP2004520703A (en) | 2004-07-08 |
DE60140753D1 (en) | 2010-01-21 |
KR20030019375A (en) | 2003-03-06 |
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