CA3156653C - Electrolyte-solution composition and secondary battery using same - Google Patents
Electrolyte-solution composition and secondary battery using same Download PDFInfo
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- CA3156653C CA3156653C CA3156653A CA3156653A CA3156653C CA 3156653 C CA3156653 C CA 3156653C CA 3156653 A CA3156653 A CA 3156653A CA 3156653 A CA3156653 A CA 3156653A CA 3156653 C CA3156653 C CA 3156653C
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0567—Liquid materials characterised by the additives
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0568—Liquid materials characterised by the solutes
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
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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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
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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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive 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
- H01M2300/00—Electrolytes
- H01M2300/0002—Aqueous electrolytes
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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
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
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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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings; Jackets or wrappings
- H01M50/102—Primary casings; Jackets or wrappings characterised by their shape or physical structure
- H01M50/109—Primary casings; Jackets or wrappings characterised by their shape or physical structure of button or coin shape
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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
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Abstract
Description
BATTERY USING SAME
FIELD OF THE INVENTION
[0001]
The present disclosure relates to an electrolyte-solution composition and a secondary battery using the same, and more particularly to an electrolyte-solution composition having a hydroxyquinoline compound and a secondary battery using the same for improving an electrical performance thereof.
BACKGROUND OF THE INVENTION
With rapid technological development nowadays, performance of consumer electronics and electric vehicles is constantly improving, and demands for energy are growing accordingly. Therefore, secondary battery becomes one of the mainstream energy storage devices with its portable and rechargeable characteristics.
Among different types of the secondary batteries, the lithium-ion secondary battery is the one having the most development potential.
Aluminum not only has advantages of high electrical conductivity, low density and low cost, but also can form a natural oxide layer (A1203) helpful for resisting corrosion on the surface. Therefore, aluminum foil is the most common choice as the cathode current collector in the lithium-ion secondary battery. However, in a lithium ion electrolyte solution, lithium salts such as lithium bis(trifluoromethanesulfonyl)imide (LiTF SI), lithium hexafluorophosphate (LiPF6) or lithium perchlorate (LiC104) still oxidize and corrode the aluminum foil. Accordingly, the dissolution of the aluminum ions occurs, and the battery performance degrades.
Date Recue/Date Received 2022-04-20
Therefore, there is a need to provide an electrolyte-solution composition having a hydroxyquinoline compound and a secondary battery using the same for improving an electrical performance thereof.
SUMMARY OF THE INVENTION
Accordingly, the capacity of the secondary battery is improved, and the occurrence of self-discharge phenomenon is avoided. The hydroxyquinoline compound further has a weight percent concentration ranged from 0.1 wt% to 2.5 wt% in the electrolyte-solution composition, so as to obtain the electrolyte-solution composition with appropriate viscosity. With the appropriate viscosity, the reduction of ionic conductivity of the electrolyte-solution composition is avoided, and the battery performance is further improved.
The electrolyte-solution composition is configured in contact with an aluminous surface of a cathode.
The electrolyte-solution composition includes an electrolyte solution and a hydroxyquinoline compound.
Date Recue/Date Received 2022-04-20
BRIEF DESCRIPTION OF THE DRAWINGS
Date Recue/Date Received 2022-04-20
Date Recue/Date Received 2022-04-20
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
Unless otherwise specified, all ranges disclosed herein are inclusive.
Date Recue/Date Received 2022-04-20
=
The molecular structure of the 5-formy1-8-hydroxyquinoline is shown below.
The present disclosure is not limited thereto.
Accordingly, the ionic conductivity of the electrolyte-solution composition 10 is reduced, and the reduction is even greater at low temperature. Therefore, the electrolyte-solution composition 10 with the appropriate viscosity is obtained by controlling the concentration of the hydroxyquinoline compound. Thereby, the reduction of the ionic conductivity of the electrolyte-solution composition is avoided, and the battery performance is further improved.
Electrolyte-solution composition Viscosity (mPa.$) Electrolyte solution 3.485 Date Recue/Date Received 2022-04-20 + 1 wt% 8-Hydroxyquinoline Electrolyte solution 3.985 + 1 wt% 5-formy1-8-Hydroxyquinoline Electrolyte solution 6.151 + 3 wt% 8-Hydroxyquinoline Electrolyte solution 6.251 + 3 wt% 5-formy1-8-Hydroxyquinoline Table 1
The present disclosure is not limited thereto.
In other embodiments, the lithium salt is one selected from the group consisting of a lithium bis(fluorosulfonyl)imide (LiFSI), a lithium hexafluorophosphate (LiPF6), a lithium perchlorate (LiC104) and a lithium metaborate (LiB04).
Date Recue/Date Received 2022-04-20
The present disclosure is not limited thereto.
Thereby, the reduction of the ionic conductivity of the electrolyte-solution composition is avoided, and the battery performance is further improved.
The test results of the following examples illustrate the efficacy of the electrolyte-solution composition of the present disclosure.
The comparative example is an electrolyte-solution composition without hydroxyquinoline compound. The electrolyte-solution composition includes a lithium bis(trifluoromethanesulfonyl)imide (LiTFSI).
Refer to FIG 2A to 2B. FIGS. 2A to 2B are SEM images illustrating surface morphology of an aluminum foil subjected to an one-week immersion test and a two-week immersion test, respectively, with the electrolyte-solution composition of the comparative example.
The Date Recue/Date Received 2022-04-20 electrolyte-solution composition only includes a LiTFSI. The LiTFSI has a concentration of 1 mol/kgw. As shown in FIG. 2A, the aluminum foil surface is significantly corroded after the one-week immersion test. As shown in FIG
2B, the aluminum foil surface is totally corroded after the two-week immersion test.
Refer to FIG 3. FIG 3 is a potentiodynamic polarization curve of the electrolyte-solution composition of the comparative example.
The electrolyte-solution composition only includes a LiTFSI. The LiTFSI has a concentration of 1 mol/kgw. The potentiodynamic polarization curve is obtained with a three-electrode system. The three-electrode system includes an aluminum foil as a working electrode, a graphite as a counter electrode, and a reversible hydrogen electrode (RHE) as a reference electrode. In the test, the potential is firstly scanned in the cathodic direction from the corrosion potential (Econ), and then scanned in the anodic direction from the corrosion potential.
Before the test, the electrodes are immersed in the electrolyte-solution composition for a few seconds to ensure a consistent corrosion potential.
Fitting results of the potentiodynamic polarization curve in FIG 3 are shown as follows. The corrosion potential is 262.89 mV. The corrosion current (Icon) is 9.60 IAA. The corrosion rate (CR) of the working electrode is 0.1116 millimeters per year (mmpy). The aluminum foil is further subjected to an Energy dispersive X-ray spectrometer (EDS) analysis after the potentiodynamic polarization test. Results of the EDS analysis show that the aluminum content on the surface of the aluminum foil is 79.08 wt%. In other words, after the potentiodynamic polarization test, about 79 wt% aluminum is remained on the surface of the aluminum foil.
Date Recue/Date Received 2022-04-20
FIGS. 4A to 4C are charging/discharging curves of a secondary battery using an electrolyte-solution composition of the comparative example at the first cycle, the fifth cycle and the fifteenth cycle. The electrolyte-solution composition only includes a LiTFSI
and a Zn(OT02. The LiTFSI has a concentration of 21 mol/kgw, and the Zn(OTO2 has a concentration of 2 mol/kgw. Preferably but not exclusively, the secondary battery is a CR2032 type coin cell. The secondary battery includes an aluminum foil coated with lithium vanadium fluorophosphates (LiVP04F, LVPF) as a cathode, a zinc foil as an anode, and a glass fiber as a separator.
The charging/discharging experiment is carried out under the room temperature (25 C) with a 40-channel battery analyzer. The charging/discharging rate (C-rate) is 2 C, and the potential window while charging/discharging is from 0.6 V to 2.2 V. Table 2 below shows the charging/discharging capacity of the secondary battery at the first cycle, the fifth cycle and the fifteenth cycle.
Table 2 also shows the capacity retention rate at the fifteenth cycle.
Capacity Fifteenth retention rate First cycle Fifth cycle cycle at fifteenth cycle Charging capacity 116.98 88.10 36.77 31.4%
(mAh/g) Discharging capacity 98.84 78.16 33.00 34.4%
(mAh/g) Table 2
Refer to FIG 7. FIG 7 is a potentiodynamic polarization curve of the electrolyte-solution composition of the first demonstrative example of the present disclosure. The electrolyte-solution composition includesa LiTFSI
anda 8-hydroxyquinoline. The LiTFSI has a concentration of 1 mol/kgw, and the 8-hydroxyquinoline has a concentration of 0.1 mol/kgw.
The potentiodynamic polarization curve is obtained with a three-electrode system.
The three-electrode system includes an aluminum foil as a working electrode, a graphite as a counter electrode, and a reversible hydrogen electrode (RHE) as a reference electrode. In the test, the potential is firstly scanned in the cathodic direction from the corrosion potential (Econ), and then scanned in the anodic direction from the corrosion potential. Before the test, the electrodes are immersed in the electrolyte-solution composition for a few seconds to ensure a consistent corrosion potential.
Fitting results of the potentiodynamic polarization curve in FIG 7 are shown as follows. The corrosion potential is 335.66 mV. The corrosion current (Icon) is 0.421 iiik. The corrosion rate (CR) of the working electrode is 4.89x10-3 millimeters per year (mmpy). The aluminum foil is further subjected to an Energy dispersive X-ray spectrometer (EDS) analysis after the potentiodynamic polarization test. Results of the EDS analysis show that the aluminum content on the surface of the aluminum foil is 84.85 wt%. In other words, after the potentiodynamic polarization test, about 85 wt% aluminum is remained on the surface of the aluminum foil.
Date Recue/Date Received 2022-04-20
FIGS. 8A to 8C are charging/discharging curves of a secondary battery using the electrolyte-solution composition of the first demonstrative example of the present disclosure at the first cycle, the fifth cycle and the fifteenth cycle. The electrolyte-solution composition includes a LiTFSI, a Zn(OTO2 and a 8-hydroxyquinoline. The LiTFSI has a concentration of 21 mol/kgw, the Zn(OTO2 has a concentration of 2 mol/kgw, and the 8-hydroxyquinoline has a concentration of 0.1 mol/kgw.
Preferably but not exclusively, the secondary battery is a CR2032 type coin cell.
The secondary battery includes an aluminum foil coated with LVPF as a cathode, a zinc foil as an anode, and a glass fiber as a separator.
The charging/discharging experiment is carried out under the room temperature (25 C) with a 40-channel battery analyzer. The charging/discharging rate (C-rate) is 2 C, and the potential window while charging/discharging is from 0.6 V to 2.2 V. Table 3 below shows the charging/discharging capacity of the secondary battery at the first cycle, the fifth cycle and the fifteenth cycle.
As shown in table 3, the secondary battery using the electrolyte-solution composition of the first demonstrative example has a charging capacity of 151.75 mAh/g and a discharging capacity of 140.31 mAh/g, which are obviously greater than those of the secondary battery using the electrolyte-solution composition of the comparative example.
First cycle Fifth cycle Fifteenth cycle Charging capacity 151.75 119.09 40.89 (mAh/g) Date Recue/Date Received 2022-04-20 Discharging capacity 140.31 115.33 39.94 (mAh/g) Table 3
and a 5-formy1-8-hydroxyquinoline. The LiTFSI has a concentration of 1 mol/kgw, and the 5-formy1-8-hydroxyquinoline has a concentration of 0.1 mol/kgw. The potentiodynamic polarization curve is obtained with a three-electrode system. The three-electrode system includes an aluminum foil as a working electrode, a graphite as a counter electrode, and a reversible hydrogen electrode (RHE) as a reference electrode. In the test, the potential is firstly scanned in the cathodic direction from the corrosion potential (Econ), and then scanned in the anodic direction from the corrosion potential. Before the test, the electrodes are immersed in the electrolyte-solution composition for a few seconds to ensure a consistent corrosion potential.
are shown as follows. The corrosion potential is 306.85 mV. The corrosion current (Icon) is 0.253 A. The corrosion rate (CR) of the working electrode is 2.94x10-3 millimeters per year (mmpy). The aluminum foil is further subjected Date Recue/Date Received 2022-04-20 to an Energy dispersive X-ray spectrometer (EDS) analysis after the potentiodynamic polarization test. Results of the EDS analysis show that the aluminum content on the surface of the aluminum foil is 86.30 wt%. In other words, after the potentiodynamic polarization test, about 86 wt% aluminum is remained on the surface of the aluminum foil.
FIGS. 12A to 12C are charging/discharging curves of a secondary battery using the electrolyte-solution composition of the second demonstrative example of the present disclosure at the first cycle, the fifth cycle and the fifteenth cycle. The electrolyte-solution composition includes a LiTFSI, a Zn(OTO2 and a 5-formy1-8-hydroxyquinoline.
The LiTFSI has a concentration of 21 mol/kgw, the Zn(OTO2 has a concentration of 2 mol/kgw, and the 5-formy1-8-hydroxyquinoline has a concentration of 0.1 mol/kgw. The secondary battery is a CR2032 type coin cell. The secondary battery includes an aluminum foil coated with LVPF as a cathode, a zinc foil as an anode, and a glass fiber as a separator. The charging/discharging experiment is carried out under the room temperature (25 C) with a 40-channel battery analyzer. The charging/discharging rate (C-rate) is 2 C, and the potential window while charging/discharging is from 0.6 V to 2.2 V. Table 4 below shows the charging/discharging capacity of the secondary battery at the first cycle, the fifth cycle and the fifteenth cycle.
Table 4 also shows the capacity retention rate at the fifteenth cycle. As shown in table 4, the secondary battery using the electrolyte-solution composition of the second demonstrative example has a charging capacity of 125.04 mAh/g and a discharging capacity of 114.57 mAh/g, which are obviously greater than those of the secondary battery using the electrolyte-solution composition of the Date Recue/Date Received 2022-04-20 comparative example. Furthermore, the secondary battery using the electrolyte-solution composition of the second demonstrative example has a charging capacity retention rate of 81.9% and a discharging capacity retention rate of 86.6%, which are also obviously greater than those of the secondary battery using the electrolyte-solution composition of the comparative example.
Capacity Fifteenth retention rate First cycle Fifth cycle cycle at fifteenth cycle Charging capacity 125.04 116.09 102.43 81.9%
(mAh/g) Discharging capacity 114.57 110.67 99.18 86.6%
(mAh/g) Table 4
Refer to FIG 13. FIG 13 is a battery characteristic curve illustrating another secondary battery using the electrolyte-solution composition of the second demonstrative example of the present disclosure. The secondary battery is charged and discharged for 5 cycles and left to sit for 24 hours.
The electrolyte-solution composition includes a LiTFSI, a Zn(0Tf)2 and a 5-formy1-8-hydroxyquinoline. The LiTFSI has a concentration of 21 mol/kgw, the Zn(0Tf)2 has a concentration of 2 mol/kgw, and the 5-formy1-8-hydroxyquinoline has a concentration of 0.1 mol/kgw.
The secondary battery is a CR2032 type coin cell. The secondary battery includes an aluminum foil coated with LVPF as a cathode, a zinc foil as an anode, and a glass fiber as a separator. The charging/discharging experiment is carried out under the room temperature (25 C) with a 40-channel battery analyzer. The Date Recue/Date Received 2022-04-20 charging/discharging rate (C-rate) is 0.2C, and the potential window while charging/discharging is from 0.6 V to 2.2 V. As shown in FIG 13, the secondary battery completes the fifth cycle at the twenty-second hour, and is left to sit for 24 hours to the forty-sixth hour. The current of the secondary battery is kept at the same level from the beginning to the end of the sitting period.
It is clear that the secondary battery using the electrolyte-solution composition of the second demonstrative example has no self-discharge phenomenon.
Date Recue/Date Received 2022-04-20
Claims (12)
an electrolyte solution; and a hydroxyquinoline compound comprising a 5-formy1-8-hydroxyquinoline.
a cathode comprising an aluminous surface; and Date Recue/Date Received 2023-05-30 an electrolyte-solution composition configured to contact the aluminous surface, wherein the electrolyte-solution composition comprises:
an electrolyte solution; and a hydroxyquinoline compound comprising a 5-formy1-8-hydroxyquinoline.
Date Recue/Date Received 2023-05-30
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| CA3156653C true CA3156653C (en) | 2023-11-21 |
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| CN116337744A (en) * | 2023-04-07 | 2023-06-27 | 江西省盛纬材料有限公司 | A Method for Evaluation of Electrolyte Resistance Performance of Aluminum-plastic Composite Film |
| KR20240161329A (en) | 2023-05-04 | 2024-11-12 | 주식회사 천보 | Electrolite composition having bis(fluorosulfony)imide alkali metal salt and corrosion inhibitor for aluminium |
| KR20250034712A (en) | 2023-09-04 | 2025-03-11 | 주식회사 천보 | Electrolite composition having bis(fluorosulfony)imide alkali metal salt and corrosion inhibitor for aluminium |
| KR20250105982A (en) | 2024-01-02 | 2025-07-09 | 주식회사 천보 | A coating agent for current collector of positive electrode comprising benzotriazole |
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| CN1170332C (en) * | 1999-02-11 | 2004-10-06 | 陆安民 | High-energy low-consumption long-life environment-protecting type lead battery and its preparation method |
| JP2009117081A (en) * | 2007-11-02 | 2009-05-28 | Asahi Kasei Chemicals Corp | Lithium ion secondary battery electrolyte and lithium ion secondary battery |
| JPWO2011052605A1 (en) | 2009-10-27 | 2013-03-21 | 旭硝子株式会社 | Nonaqueous electrolyte for secondary battery and secondary battery |
| JP5680468B2 (en) | 2010-09-22 | 2015-03-04 | 富士フイルム株式会社 | Non-aqueous secondary battery electrolyte and lithium secondary battery |
| CN102340029A (en) | 2011-09-22 | 2012-02-01 | 合肥国轩高科动力能源有限公司 | A functional additive for non-aqueous electrolytes of lithium-ion batteries |
| JP2016213101A (en) | 2015-05-12 | 2016-12-15 | 株式会社テクノバ | Aluminum secondary battery |
| CN108091489B (en) * | 2016-11-23 | 2021-03-26 | 东莞东阳光科研发有限公司 | Working electrolyte of 850-plus-900V aluminum electrolytic capacitor and preparation method thereof |
| WO2018135395A1 (en) * | 2017-01-20 | 2018-07-26 | 富士フイルム株式会社 | Electrolytic solution for non-aqueous secondary batteries, non-aqueous secondary battery, and metal complex |
| WO2021038922A1 (en) * | 2019-08-23 | 2021-03-04 | 日本碍子株式会社 | Lithium ion secondary battery |
| CN112635822B (en) * | 2019-09-24 | 2021-11-09 | 宁德时代新能源科技股份有限公司 | Lithium ion battery |
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| KR102769546B1 (en) | 2025-02-17 |
| CN115275338A (en) | 2022-11-01 |
| TWI834150B (en) | 2024-03-01 |
| JP2022171591A (en) | 2022-11-11 |
| CA3156653A1 (en) | 2022-10-29 |
| US12249691B2 (en) | 2025-03-11 |
| AU2022202603B2 (en) | 2023-05-25 |
| AU2022202603A1 (en) | 2022-11-17 |
| EP4084154A1 (en) | 2022-11-02 |
| US20220367912A1 (en) | 2022-11-17 |
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