WO2013164525A1 - Systeme d'accumulateurs et piles aluminium air - Google Patents
Systeme d'accumulateurs et piles aluminium air Download PDFInfo
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- WO2013164525A1 WO2013164525A1 PCT/FR2013/050766 FR2013050766W WO2013164525A1 WO 2013164525 A1 WO2013164525 A1 WO 2013164525A1 FR 2013050766 W FR2013050766 W FR 2013050766W WO 2013164525 A1 WO2013164525 A1 WO 2013164525A1
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- cell
- electrolyte
- air
- aluminum
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/08—Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/04—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
- H01M12/06—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
- H01M12/065—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode with plate-like electrodes or stacks of plate-like electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0025—Organic electrolyte
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0085—Immobilising or gelification of electrolyte
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Definitions
- the present invention relates to the field of storage of electrical energy, in particular the field of electrochemical metal-air cells.
- the storage of electrical energy including batteries are increasingly used and for increasingly diverse applications: mobile phones, laptops, portable tools, electric vehicles or hybrids ...
- the energy storage means must be light, compact and must satisfy the electrical characteristics associated with their use.
- a metal-air electrochemical cell consists of a negative electrode (anode) where the metal will be the seat of an oxidation reaction during the discharge of the cell, while the positive electrode (cathode, also called electrode to air) involves a reduction reaction of the oxygen contained in the air, an electrolyte ensures the ionic conduction between electrodes by means of ionic species.
- the air electrode is most often made of an assembly of two active layers containing a catalyst that sandwich a metal grid.
- Lithium is the most electronegative and lightest element of metals; Naturally a lot of development work is underway on Li-air batteries, as shown for example in US patent application 2009/0053594 A1.
- lithium is a material that can present a number of hazards when exposed to ambient air and, if the natural reserves of this metal are important, the costs of extraction and treatment are also important.
- the massive use of lithium in Li-ion batteries tends to reduce these reserves.
- Silicon is also of increasing interest and patent application WO 201 1/061728 A1 describes a system of this type. In this document, the silicon used is doped n-type or p, which is a relatively high additional cost, even if the implementation technologies are perfectly mastered for microelectronics.
- Aluminum is a trivalent metal of low atomic mass, abundant, which presents no danger when exposed to the air and relatively inexpensive.
- Aluminum-air battery systems or mechanically rechargeable aluminum-air batteries are described in the prior art, in particular in the patent applications WO 2010/132357 and WO 2002/086984.
- the aluminum-air systems described in the prior art involve an electrolyte comprising a saline solution or a solution alkaline. In the latter case, which has been most studied, the reaction of reduction of oxygen in water at the cathode generates hydroxyl ions. The oxidation of the metal in the presence of these ions causes the formation of crystalline hydrated aluminum hydroxide which precipitates and progressively clogs the pores of the air cathode, which results in a degradation of the performance of the electrochemical cell.
- the first document indicates the possibility that the metal electrode is aluminum and describes different types of electrolytes that can be used, but does not provide a solution to the problems encountered with aluminum-air systems.
- the patent application WO 2002/086984 proposes to use a "desiccant" additive that will prevent the formation of crystalline hydrated aluminum hydroxide to give a compound crystallizing with fewer molecules. of water, which has the effect of increasing the duration of use of the battery.
- adding an additive increases the cost of the cell.
- the conductivity of the electrolyte is decreased by adding additives. Indeed, among the organic additives claimed in this document, starch and polyacrylamide will increase the viscosity of the medium (formation of a gel), thus reducing the conductivity. The other two additives will decrease the amount of water present in the electrolyte and make it less conductive.
- a second problem of aluminum-air cells is related to the phenomenon of aluminum corrosion observed in alkaline media and which results in a release of hydrogen with the safety problems that this entails and significant overvoltages which penalize the overall performance. of the pile. Neither of these two documents solves this problem; for example, the addition of additive does not reduce the release of hydrogen related to the corrosion of aluminum.
- the invention relates to an electrochemical cell aluminum-air comprising an electrolyte which is non-aqueous and which is, by its composition, little corrosive vis-à-vis aluminum.
- an electrochemical cell aluminum-air equipped with such an electrolyte is light, with good electrochemical performance while having suitable electrical characteristics for the storage of electrical energy.
- the invention relates to an electrochemical aluminum-air cell capable of supplying and / or accumulating electrical energy comprising an oxidizable electrode made of aluminum or aluminum alloy, a conductive air electrode allowing air diffusion and reduction. oxygen from the air and an electrolyte.
- the electrolyte is non-aqueous, and includes a mixture of aluminum trichloride (A / C7 3 ) with a chlorinated aliphatic, cyclic or heterocyclic nitrogen derivative.
- the molar ratio of the amount of aluminum trichloride (AlCl 3 ) to the amount of chlorinated aliphatic, cyclic or heterocyclic nitrogen derivative is between 1, 01 and 2.
- the chlorinated aliphatic, cyclic or heterocyclic nitrogen-containing derivative of the electrolyte is chosen from 1-ethyl-3-methyl-imidazolium chloride (EMImCl), 1-butyl-3-methyl-imidazolium chloride, and 1-butyl-pyridinium, or benzyltrimethylammonium chloride.
- EMImCl 1-ethyl-3-methyl-imidazolium chloride
- 1-butyl-3-methyl-imidazolium chloride 1-butyl-3-methyl-imidazolium chloride
- 1-butyl-pyridinium 1-butyl-pyridinium
- benzyltrimethylammonium chloride 1-ethyl-3-methyl-imidazolium chloride
- the molar ratio of the amount of aluminum trichloride to the amount of 1-ethyl-3-methyl-imidazolium chloride (EMImCl) is substantially equal to 1.5.
- said electrolyte further comprises an organic liquid and / or an ionic liquid.
- said electrolyte is liquid at ambient temperature of use of the cell.
- said electrolyte is a room temperature gel for use of the cell.
- said air electrode comprises a microporous multilayer assembly and an active element allowing the reduction of oxygen.
- said air electrode consists of porous carbon, an oxygen reduction catalyst, perfluorinated polymer and a current collector.
- said oxygen reduction catalyst is chosen from metal oxides, in particular oxides of manganese, nickel or cobalt or from doped metal oxides, or from noble metals.
- the cell may further comprise porous devices located upstream of the air electrode.
- the invention relates to an electrochemical system for storing electrical energy, consisting of at least one cell according to the invention.
- the electrochemical system for storing the electrical energy comprises a plurality of cells as described above, arranged in series and / or in parallel.
- the invention relates to a vehicle, in particular a motor vehicle, comprising at least one electric machine.
- vehicle is equipped with an electrical energy storage system according to the invention for powering said electric machine.
- FIG. 1 illustrates an electrochemical aluminum-air cell according to the invention, used experimentally.
- Figure 2 illustrates discharge curves of an electrochemical cell according to the invention.
- FIG. 3 illustrates load and discharge curves of an electrochemical cell according to the invention.
- the invention therefore relates to an electrolyte for a metal-air electrochemical cell capable of supplying and / or accumulating electrical energy.
- this electrolyte is non-aqueous, which makes it possible to avoid the formation of crystalline hydrated aluminum hydroxide, which can clog the pores of the air electrode of the electrochemical cell.
- the performance of the cell degrades less in time than the cells envisaged in the prior art.
- the electrolyte comprises a mixture of a chlorinated aliphatic, cyclic or heterocyclic nitrogen derivative with aluminum trichloride (A / C7 3 ).
- This mixture is slightly corrosive to aluminum, as experimentally verified (corrosion measurements are described in Example 1).
- the electrolyte according to the invention can therefore be used in an electrochemical aluminum-air cell, while at the same time avoiding the formation of aluminum hydroxide and, secondly, by reducing the corrosion of the metal electrode, this which therefore allows a decrease in hydrogen evolution.
- the chlorinated aliphatic, cyclic or heterocyclic nitrogen compound which is mixed in the electrolyte with aluminum trichloride may be chosen from 1-ethyl-3-methyl-imidazolium chloride, chloride 1-butyl-3-methylimidazolium, 1-butyl-pyridinium chloride, or benzyltrimethylammonium chloride.
- Other compounds that can be used are described in "Electrodeposition from ionic liquids" edited by F. Endres, D. MacFarlane and A. Abbott, Wiley-VCH (2008). More generally, it is possible to use any mixture of an ionic salt with AICI 3 which makes it possible to obtain an ionic conductive liquid electrolyte which has an electrochemical window sufficient to effect this reaction.
- the non-aqueous electrolyte is at room temperature a liquid or a gel.
- the gels are adapted as electrolytes.
- the electrolyte may further contain an ionic solution whose purpose is to ensure the stability of the gel at high temperature (about 60 ° C).
- the molar ratio of aluminum trichloride AlCl 3 to the chlorinated nitrogen derivative is between 1.0 and 2, and has very low corrosion with respect to aluminum. Indeed, this ratio ensures a high concentration of aluminum ions, which promotes the diffusion of ionic species (high transport number) with high current densities and which allows a high specific power.
- the electrolyte may further comprise ionic and / or organic liquids.
- This type of electrolyte is particularly little corrosive with respect to aluminum under the normal conditions of use of electrochemical cells (see Example 1).
- electrolyte it is possible to construct an electrochemical aluminum-air cell, in which the evolution of hydrogen is reduced (because the phenomenon of corrosion is limited), and in which no aluminum hydroxide is form.
- This electrochemical system consists of an assembly comprising a metal component (metal electrode) capable of undergoing an oxidation reaction, consisting of aluminum or an aluminum alloy, of a non-aqueous electrolyte with very little corrosive to the metal or metal alloy and an electrode (called air electrode) for the reduction of oxygen.
- the air electrode may comprise a microporous multilayer assembly for the diffusion of gases and may comprise at least one active element for the reduction of oxygen.
- the air electrodes are made of porous carbon, perfluorinated polymer such as PTFE, PFA, FEP ... and comprise an oxygen reduction catalyst and a current collector.
- the oxygen reduction catalyst is chosen from metal oxides such as oxides of manganese, nickel or cobalt for example, doped metal oxides, or from noble metals such as platinum, palladium, or silver.
- the electrochemical cell works indifferently with pure oxygen, with a mixture of oxygen and nitrogen or with air. It is also possible to add to the cell porous devices located upstream of the air electrode, to remove water and / or carbon dioxide from the air.
- the geometry of the assembly is not a brake on the operation of the electrochemical cell if a sufficient flow of oxygen is maintained for the proper functioning of the assembly. Consequently, any type of geometry of the cell is adapted to the invention: the cell can be cylindrical (concentric electrodes), parallelepipedal (parallel electrodes) ... It is also possible to use an inert porous separator (for example woven polypropylene or non-woven, microporous, PTFE ”) which provides electrical insulation between the two electrodes.
- an inert porous separator for example woven polypropylene or non-woven, microporous, PTFE
- the electrochemical cell according to the invention comprises a single electrolyte, adapted to the two electrodes (in particular non-corrosive with respect to aluminum) and having good electrochemical characteristics.
- a cell constitutes an electrochemical storage system for electrical energy, for example in the form of a battery.
- an electrochemical storage system for electrical energy is constructed, in particular a rechargeable battery, or accumulator system (see Example 3).
- the series and / or parallel assembly depends on the desired electrical characteristics (voltages, currents, powers, etc.) for the application of the energy storage system.
- This electrochemical energy storage system can be used as an onboard battery in vehicles; for example, motor vehicles or electric or hybrid two-wheelers. However, this system is also suitable for use for mobile phones, laptops, portable tools in which a battery is shipped.
- Example 1 In order to establish the non-corrosivity of the electrolyte vis-à-vis the metal component of the electrochemical cell, the applicant conducted an experiment to measure the corrosion of aluminum by the electrolyte according to the invention.
- EMImCl 1-ethyl-3-methyl-imidazolium chloride
- Solvionic® 1-ethyl-3-methyl-imidazolium chloride
- AlCl 3 dry aluminum chloride
- the measurement of corrosion is carried out in a glove box using an SP 150 potentiostat from Biologie ®, and visualization and data processing using the EC-Lab ® software.
- a 1 mm diameter aluminum wire marketed by GoodFellow® with a purity of 99.9999%
- a reference electrode or quasi-reference
- Electrochemical measurement by linear polarization is carried out by a scanning of
- the Tafel curves which are curves of the logarithm of the current as a function of the voltage, are then drawn in. These curves give a cathodic line ( oxygen or proton reduction reaction) and an anodic straight line (oxidation of the metal) on either side of the corrosion potential. The corrosion current is then deduced by the coordinates of the point of intersection of these 2 straight lines.
- the plot of the Tafel curves makes it possible to determine, for this experiment, a corrosion current density of less than 3 ⁇ . ⁇ "2 . This value is extremely low and shows that the electrolyte is particularly low corrosive vis-à-vis aluminum under the conditions of the experiment.
- Figure 1 illustrates the mounting of the cell for measurements.
- a glove box we assemble, on a metal support (5) covered with an insulating coating and equipped with an air vent (8), the body of the cell (4) made of PTFE equipped with other seals and an opening (7) permitting injecting the electrolyte between an aluminum plate (2) and an air electrode (1).
- a tightening handle (6) ensures the tight assembly of the assembly.
- the distance between the aluminum plate (2) and the air electrode (1) is 10 mm for an internal diameter of the body of the cell of 15 mm.
- the complete assembly containing the electrolyte (3) is introduced into a glass cell comprising: two sealed outlets allowing the electrical connection to a potentiostat, an arrival of dry air freed of carbon dioxide by means of a guard of 5X molecular sieve.
- the air supply rate of the cell is set at 30 ml / min.
- the galvanostatic discharge manipulations were carried out using an SP 150 potentiostat from BioLogic ®, visualization and data processing using the EC-Lab ® software.
- the discharge measurements were performed for different current densities: -50 ⁇ . ⁇ 2 ; -100 ⁇ . ⁇ 2 ; -300 ⁇ . ⁇ 2 ; and -600 ⁇ . ⁇ 2 at a temperature of 22 ⁇ C ⁇ 3 ° C.
- the curves of discharges obtained are represented in FIG. 2. These curves represent the evolution of the voltage U (in V) at the terminals of the cell as a function of time t (in days).
- the results obtained show that the electrochemical aluminum-air system allows in a non-corrosive aprotic medium to obtain energy generation from aluminum and oxygen from the air.
- the values in the table are determined for a current density of -100 ⁇ . ⁇ 2 .
- the first example (lithium electrode) is shown in particular in the document: Takashi Kuboki, Tetsuo Okuyama, Takahisa Ohsaki, Norio Takami, "Lithium-air batteries using hydrophobic room temperature ionic liquid electrolyte", Journal of Power Sources 146, 766-769 (2005).
- the second example silicon electrode
- the values are calculated using the data from the document: Gil Cohn, Yair Ein-Eli, "Study and development of non-aqueous silicon-air battery", Journal of Power Sources 195, 4963-4970 (2010).
- the capacity / carbon is calculated taking into account the mass of carbon and the catalyst of the air electrode, this capacity corresponds to the capacity of the cell per unit mass. It should be noted that the cell according to the invention makes it possible to construct a cell having a higher capacity / carbon than the lithium-air or silicon-air cells described in the literature.
- a cell identical to the cell formed in Example 2 is constructed. This cell is subjected to several cycles of charging and discharging by imposing a current to the cell.
- Figure 3 illustrates the behavior of the cell for these charge and discharge cycles.
- the curve in solid line corresponds to the voltage U at the terminals of the cell.
- the curve in dashed lines corresponds to the current I imposed on the cell. These curves represent the evolution of the voltage U (in V) and the current I (in mA / cm 2 ) at the terminals of the cell as a function of time t (in hours).
- a positive direct current (+0.6 mA / cm 2 ) is applied in charge and negative (-0.6 mA cm 2 ) in discharge.
- the cell according to the invention is adapted for a rechargeable battery (battery).
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- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
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Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015509470A JP2015521344A (ja) | 2012-05-04 | 2013-04-09 | アルミニウム−空気電池および蓄電池システム |
EP13720463.2A EP2845262A1 (fr) | 2012-05-04 | 2013-04-09 | Systeme d'accumulateurs et piles aluminium air |
CN201380023619.8A CN104303360A (zh) | 2012-05-04 | 2013-04-09 | 包括蓄电池和空-铝电池组的系统 |
KR1020147033602A KR20150018527A (ko) | 2012-05-04 | 2013-04-09 | 축전지들 및 공기-알루미늄 배터리들을 포함하는 시스템 |
CA2869911A CA2869911A1 (fr) | 2012-05-04 | 2013-04-09 | Systeme d'accumulateurs et piles aluminium air |
US14/398,481 US20150093659A1 (en) | 2012-05-04 | 2013-09-04 | Aluminium-air battery and accumulator system |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1201303A FR2990304B1 (fr) | 2012-05-04 | 2012-05-04 | Systeme d'accumulateurs et piles aluminium air |
FR12/01.303 | 2012-05-04 |
Publications (1)
Publication Number | Publication Date |
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WO2013164525A1 true WO2013164525A1 (fr) | 2013-11-07 |
Family
ID=48289452
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2013/050766 WO2013164525A1 (fr) | 2012-05-04 | 2013-04-09 | Systeme d'accumulateurs et piles aluminium air |
Country Status (8)
Country | Link |
---|---|
US (1) | US20150093659A1 (fr) |
EP (1) | EP2845262A1 (fr) |
JP (1) | JP2015521344A (fr) |
KR (1) | KR20150018527A (fr) |
CN (1) | CN104303360A (fr) |
CA (1) | CA2869911A1 (fr) |
FR (1) | FR2990304B1 (fr) |
WO (1) | WO2013164525A1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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FR3031625A1 (fr) * | 2015-01-08 | 2016-07-15 | Peugeot Citroen Automobiles Sa | Procede de fabrication d’une electrode negative par compression d’une pate et d’une mousse metalliques, pour un dispositif de stockage d’energie electrique |
JP2016213964A (ja) * | 2015-05-08 | 2016-12-15 | シャープ株式会社 | 電池システム、電極カートリッジ、放電槽、電池及び充電槽 |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109524617A (zh) * | 2014-03-31 | 2019-03-26 | 泰克年研究发展基金会公司 | 钝态金属活化方法和其用途 |
WO2016160703A1 (fr) | 2015-03-27 | 2016-10-06 | Harrup Mason K | Solvants entièrement inorganiques pour électrolytes |
ES2540171B1 (es) | 2015-04-29 | 2016-04-21 | Albufera Energy Storage, S.L. | Celda electroquímica de aluminio-manganeso |
CN106548878B (zh) * | 2015-09-22 | 2018-08-10 | 南京绿索电子科技有限公司 | 一种使用离子液体电解液的超级电容器 |
CN105406074A (zh) * | 2015-12-09 | 2016-03-16 | 江苏科技大学 | 一种正极为石墨烯复合电极的二次离子电池及制备方法 |
ES2636362B1 (es) * | 2016-04-05 | 2018-07-18 | Albufera Energy Storage, S.L. | Celda electroquímica aluminio-aire recargable |
US10707531B1 (en) | 2016-09-27 | 2020-07-07 | New Dominion Enterprises Inc. | All-inorganic solvents for electrolytes |
CA3046940A1 (fr) | 2016-12-15 | 2018-06-21 | Phinergy Ltd. | Systeme et procede pour initialiser et faire fonctionner une pile metal-air |
TWI654170B (zh) | 2017-12-22 | 2019-03-21 | 財團法人工業技術研究院 | 電解質組成物及包含其之金屬離子電池 |
US10340552B1 (en) | 2017-12-22 | 2019-07-02 | Industrial Technology Research Institute | Electrolyte composition and metal-ion battery employing the same |
CN108933310B (zh) * | 2018-05-25 | 2021-07-02 | 四川大学 | 一种高容量高功率型锂离子/空气混合电池系统 |
KR102246948B1 (ko) * | 2020-02-05 | 2021-04-30 | 부산대학교 산학협력단 | 에너지 효율이 향상된 알루미늄-공기 전지의 제조 방법 |
CN112002937A (zh) * | 2020-08-07 | 2020-11-27 | 山东科技大学 | 一种用于铝离子电池的凝胶电解质及其制备方法和应用 |
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2012
- 2012-05-04 FR FR1201303A patent/FR2990304B1/fr not_active Expired - Fee Related
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2013
- 2013-04-09 EP EP13720463.2A patent/EP2845262A1/fr not_active Withdrawn
- 2013-04-09 JP JP2015509470A patent/JP2015521344A/ja active Pending
- 2013-04-09 WO PCT/FR2013/050766 patent/WO2013164525A1/fr active Application Filing
- 2013-04-09 CA CA2869911A patent/CA2869911A1/fr not_active Abandoned
- 2013-04-09 KR KR1020147033602A patent/KR20150018527A/ko not_active Application Discontinuation
- 2013-04-09 CN CN201380023619.8A patent/CN104303360A/zh active Pending
- 2013-09-04 US US14/398,481 patent/US20150093659A1/en not_active Abandoned
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3031625A1 (fr) * | 2015-01-08 | 2016-07-15 | Peugeot Citroen Automobiles Sa | Procede de fabrication d’une electrode negative par compression d’une pate et d’une mousse metalliques, pour un dispositif de stockage d’energie electrique |
JP2016213964A (ja) * | 2015-05-08 | 2016-12-15 | シャープ株式会社 | 電池システム、電極カートリッジ、放電槽、電池及び充電槽 |
Also Published As
Publication number | Publication date |
---|---|
FR2990304A1 (fr) | 2013-11-08 |
CA2869911A1 (fr) | 2013-11-07 |
EP2845262A1 (fr) | 2015-03-11 |
FR2990304B1 (fr) | 2014-04-25 |
CN104303360A (zh) | 2015-01-21 |
JP2015521344A (ja) | 2015-07-27 |
US20150093659A1 (en) | 2015-04-02 |
KR20150018527A (ko) | 2015-02-23 |
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