WO2016006315A1 - 3,3,3-トリフルオロプロピオネート基を有するエステルを含む非水電解液、及びそれを用いた非水電解液電池 - Google Patents
3,3,3-トリフルオロプロピオネート基を有するエステルを含む非水電解液、及びそれを用いた非水電解液電池 Download PDFInfo
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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
- H01M10/0569—Liquid materials characterised by the solvents
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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
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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
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0025—Organic electrolyte
- H01M2300/0028—Organic electrolyte characterised by the solvent
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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
- H01M2300/0028—Organic electrolyte characterised by the solvent
- H01M2300/0037—Mixture of solvents
- H01M2300/004—Three solvents
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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
Definitions
- the present invention relates to a novel non-aqueous electrolyte and a non-aqueous electrolyte secondary battery including the non-aqueous electrolyte.
- an ester having a 3,3,3-trifluoropropionate group at both ends represented by the following general formula 1, a fluorinated cyclic carbonate that is 4-fluoroethylene carbonate (FEC) or a derivative thereof, and a cyclic carbonate
- FEC 4-fluoroethylene carbonate
- the present invention relates to a non-aqueous electrolyte containing at least one selected from chain carbonates and fluorinated chain carboxylic acid esters, and a non-aqueous electrolyte secondary battery using the non-aqueous electrolyte.
- Non-aqueous electrolyte secondary batteries such as lithium secondary batteries, which have been used as power sources for so-called portable electronic devices such as mobile phones and notebook computers, have been increasing the performance of portable electronic devices and driving automobiles. Further expansion of the range of application to automotive on-board power sources, etc., demands higher performance and higher energy density.
- the electrolyte used for such a non-aqueous electrolyte secondary battery is usually mainly composed of an electrolyte and a non-aqueous solvent.
- a non-aqueous solvent a mixed solvent in which a cyclic carbonate such as ethylene carbonate and a chain carbonate such as diethyl carbonate, ethyl methyl carbonate, and dimethyl carbonate are mixed is used, and LiPF 6 or LiBF 4 is used as the mixed solvent.
- a solution in which a lithium salt such as is dissolved is used.
- fluorinated cyclic carbonates such as 4-fluoroethylene carbonate are less stable than vinylene carbonate, which is generally known as a polymer film forming additive for negative electrodes.
- Deterioration of battery capacity resulting from the reforming reaction and gas generation during long-term storage and high-temperature storage are problems.
- vinylene carbonate is an outstanding polymer film formation additive, since it is inferior in oxidation resistance, the oxidative decomposition reaction in the positive electrode side has become a problem.
- a compound having both excellent oxidation resistance and an effect as a polymer film forming additive that contributes to improvement of battery characteristics of a lithium secondary battery is desired.
- the present invention has been made to solve the above-described problems, and has excellent oxidation resistance, a reaction between a non-aqueous electrolyte and an electrode, and a high voltage at which decomposition is significant in a conventional non-aqueous electrolyte. It is an object of the present invention to provide a non-aqueous electrolyte for a secondary battery that suppresses capacity deterioration even under use conditions such as conditions, and a non-aqueous electrolyte secondary battery using the non-aqueous electrolyte.
- An ester having a 3,3,3-trifluoropropionate group at both ends represented by the formula, a fluorinated cyclic carbonate which is 4-fluoroethylene carbonate (FEC) or a derivative thereof, a cyclic carbonate, a chain carbonate and fluorine
- a non-aqueous electrolyte for a secondary battery comprising: a non-aqueous solvent containing at least one selected from a chain-chain carboxylic acid ester; and a lithium salt as an electrolyte.
- the ester having a 3,3,3-trifluoropropionate group at both ends is represented by the following formula 2:
- Non-aqueous electrolysis for a secondary battery characterized in that it is at least one selected from tetramethylene bis (3,3,3-trifluoropropionate) represented by liquid.
- the ester having a 3,3,3-trifluoropropionate group at both ends is contained in the range of 0.01 to 5 vol% with respect to the whole non-aqueous solvent.
- the nonaqueous electrolyte for secondary batteries as described.
- the fluorinated cyclic carbonate which is 4-fluoroethylene carbonate (FEC) or a derivative thereof is contained in the range of 0.1 to 30 vol% with respect to the entire non-aqueous solvent.
- the nonaqueous electrolyte for secondary batteries as described.
- the fluorinated chain carboxylic acid ester includes methyl 3,3,3-trifluoropropionate CF 3 CH 2 COOCH 3 , acetic acid 2,2,2-trifluoroethyl CH 3 COOCH 2 CF 3 and these
- the non-aqueous electrolyte for secondary batteries according to [1] wherein the non-aqueous electrolyte is for at least one selected from a mixture of [6] A negative electrode and a positive electrode capable of occluding and releasing lithium, and the non-aqueous electrolyte for a secondary battery according to any one of [1] to [5] Water electrolyte secondary battery.
- the non-aqueous electrolyte for secondary battery of the present invention has excellent oxidation resistance, suppresses the reaction between the non-aqueous electrolyte and the electrode, suppresses decomposition even under high voltage conditions, and degrades the capacity of the secondary battery. And gas generation can be suppressed.
- the graph which shows the result of the cyclic voltammetry (henceforth "CV") measurement of the 3 electrode type test cell of the comparative example 1 which does not contain ethylenebis (3,3,3- trifluoropropionate) in a non-aqueous solvent. It is. It is a graph which shows the result of the CV measurement of the 3 electrode type test cell of Example 1 which contains ethylenebis (3,3,3-trifluoropropionate) in a non-aqueous solvent.
- CV cyclic voltammetry
- an ester having a 3,3,3-trifluoropropionate group at both ends represented by the following formula 1, a fluorinated cyclic carbonate that is 4-fluoroethylene carbonate (FEC) or a derivative thereof
- FEC 4-fluoroethylene carbonate
- a non-aqueous electrolyte for a secondary battery containing a lithium salt of an electrolyte in a non-aqueous solvent comprising: at least one selected from cyclic carbonate, chain carbonate, and fluorinated chain carboxylic acid ester;
- a non-aqueous electrolyte secondary battery including an aqueous electrolyte is provided.
- An ester having a 3,3,3-trifluoropropionate group at both ends represented by Formula 1 is a 3,3,3-trifluoropropionate group that can take a fluorine-containing acrylate structure by deprotonation at the ⁇ -position.
- a polymer film having an effect of improving the battery characteristics of the lithium secondary battery can be formed on the negative electrode of the lithium secondary battery, and the oxidation resistance is also excellent.
- the polymer film comprises a positive electrode capable of occluding and releasing lithium, a negative electrode capable of occluding and releasing lithium, a separator, and a non-aqueous electrolyte.
- the nonaqueous electrolytic solution of the present invention containing a lithium salt of an electrolyte is used as a nonaqueous solvent containing an ester having a 3,3,3-trifluoropropionate group at both ends, thereby allowing nonaqueous electrolysis. It is formed when the liquid secondary battery is charged for the first time.
- the above-mentioned polymer film formed on the negative electrode can suppress the reaction between the nonaqueous electrolyte and the negative electrode, and can obtain good battery characteristics.
- an appropriate polymer film is not formed, a decomposition reaction of the non-aqueous electrolyte occurs on the negative electrode, and battery characteristics deteriorate.
- lithium is not inserted into or extracted from the negative electrode.
- the amount of the ester having 3,3,3-trifluoropropionate groups at both ends in the non-aqueous solvent is small, a sufficient film cannot be formed on the negative electrode.
- the amount of the ester is too large, battery characteristics are deteriorated due to excessive film formation and a decrease in conductivity accompanying an increase in the viscosity of the non-aqueous electrolyte. Therefore, the amount of the ester having 3,3,3-trifluoropropionate groups at both ends is preferably in the range of 0.01 to 5 vol%, particularly 0.05 to 3 vol% with respect to the whole non-aqueous solvent. % Is preferable.
- ester having a 3,3,3-trifluoropropionate group at both ends examples include ethylenebis (3,3,3-trifluoropropionate) represented by the following formula 2, It is preferable to use at least one selected from tetramethylene bis (3,3,3-trifluoropropionate) represented by Formula 3 and mixtures thereof. It is more preferable to use ethylene bis (3,3,3-trifluoropropionate) represented by the following formula 2 because excessive film formation and increase in viscosity of the non-aqueous electrolyte are small.
- Esters having 3,3,3-trifluoropropionate groups at both ends have 3,3,3-trifluoropropionate groups only at one end, such as methyl 3,3,3-trifluoropropionate Compared with the conventional ester, the stability of the polymer film formed on the negative electrode of the lithium secondary battery is high, and the capacity retention rate of the cycle characteristics of the nonaqueous electrolyte secondary battery is improved.
- the above-mentioned non-aqueous solvent may further contain a high dielectric constant solvent and a low viscosity solvent.
- a high dielectric constant solvent include ethylene carbonate, propylene carbonate, 4-fluoroethylene carbonate and the like.
- Preferred examples of the low viscosity solvent include dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, ethyl acetate, methyl propionate, 2,2,2-trifluoroethyl acetate, methyl 3,3,3-trifluoropropionate and the like. Can do.
- 4-fluoroethylene carbonate, acetic acid 2,2,2-trifluoroethyl acetate, 3,3, which are fluorinated solvents, can improve the oxidation resistance of the non-aqueous electrolyte under high voltage conditions.
- acetic acid 2,2,2-trifluoroethyl acetate, 3,3, which are fluorinated solvents can improve the oxidation resistance of the non-aqueous electrolyte under high voltage conditions.
- methyl 3-trifluoropropionate Preferably methyl 3-trifluoropropionate.
- 4-Fluoroethylene carbonate which is the fluorinated solvent, can be reduced and decomposed at the negative electrode to form a polymer film.
- the amount of 4-fluoroethylene carbonate can be used as an additive for forming a polymer film by setting the amount of 4-fluoroethylene carbonate to, for example, 0.05 to 3 vol% with respect to the entire non-aqueous solvent.
- a composite polymer film formed from an ester having 3,3,3-trifluoropropionate groups at both ends represented by Formula 1 and 4-fluoroethylene carbonate is a further reduction of 4-fluoroethylene carbonate. In order to suppress decomposition, it is possible to improve cycle characteristics and to suppress gas generation.
- the non-aqueous solvent further contains 4-fluoroethylene carbonate, which is a fluorinated solvent
- 4-fluoroethylene carbonate which is a fluorinated solvent
- the amount of 4-fluoroethylene carbonate is small, a polymer film formed from 4-fluoroethylene carbonate on the negative electrode is not sufficiently formed, Battery characteristics deteriorate due to reductive decomposition of other non-aqueous solvents or excessive film formation.
- the amount of 4-fluoroethylene carbonate is preferably in the range of 0.05 to 40 vol%, more preferably in the range of 0.1 to 30 vol% with respect to the entire non-aqueous solvent.
- the potential of the positive electrode is set to 4.35 V or more on the basis of metallic lithium
- 4-fluoroethylene carbonate as a high dielectric constant solvent is used from the viewpoint of improving the oxidation resistance of the non-aqueous electrolyte under high voltage conditions.
- a fluorinated carboxylic acid ester as a low-viscosity solvent are preferably used.
- such fluorinated carboxylic acid esters include methyl 3,3,3-trifluoropropionate CF 3 CH 2 COOCH 3 , 2,2,2-trifluoroethyl acetate CH 3 COOCH 2 CF 3 or the like can be preferably used.
- examples of the electrolyte made of a lithium salt dissolved in the nonaqueous solvent include LiPF 6 , LiPO 2 F 2 , LiBF 4 , LiClO 4 , LiN (CF 3 SO 2 ) 2 , LiN (FSO 2 ) 2 , LiCF 3 SO 3 , LiC (CF 3 SO 2 ) 3 , LiC (FSO 2 ) 3 , LiCF 3 CO 2 , LiB (CF 3 SO 3 ) 4 , LiB (FSO 3 ) 4 , LiB (C 2 O 4 ) 2 , LiBF 2 (C 2 O 4 ), or the like can be used.
- the positive electrode active material used for the positive electrode of the non-aqueous electrolyte secondary battery of the present invention is not particularly limited as long as it is a material that can occlude and release lithium and has a noble potential, and is commonly used.
- the positive electrode active material can be used. Examples thereof include metal compounds such as metal oxides, metal hydroxides, metal sulfides, metal halides, and metal phosphate compounds.
- a lithium transition metal composite oxide having a layered structure such as a metal intercalation compound, a spinel structure, or an olivine structure can be used.
- Preferred examples of the transition metal element include nickel, cobalt, manganese, titanium, and iron.
- a transition metal composite oxide obtained by adding or replacing lithium, magnesium, aluminum, or titanium to these transition metal elements may be used.
- a lithium transition metal composite oxide having a layered structure in order to obtain a non-aqueous electrolyte secondary battery with high energy density, it is preferable to use a lithium transition metal composite oxide having a layered structure. Specific examples include lithium / cobalt composite oxide, lithium / cobalt / nickel / manganese composite oxide, and lithium / cobalt / nickel / aluminum composite oxide.
- the negative electrode active material used for the negative electrode of the nonaqueous electrolyte secondary battery of the present invention is not particularly limited as long as it is a material capable of occluding and releasing lithium, and a commonly used negative electrode active material that is generally used Can be used.
- lithium metal such as lithium metal, lithium-silicon alloy, lithium-tin alloy, tin-silicon alloy, lithium-titanium alloy, tin-titanium alloy, titanium oxide, carbon material, conductive polymer, etc.
- the carbon material include carbon materials such as graphite (natural, artificial), coke (petroleum, coal), fullerene, carbon nanotube, carbon fiber, and organic fired body.
- tin-based compound or the titanium-based compound a metal oxide having a potential lower than that of the positive electrode active material such as SnO 2 , SnO, or TiO 2 can be used.
- a carbon material such as crystalline graphite which has a small volume change associated with insertion and extraction of lithium and is excellent in reversibility.
- a separator for preventing a short circuit is interposed between the positive electrode and the negative electrode.
- the non-aqueous electrolyte is used by impregnating the separator.
- the material and shape of the porous film are not particularly limited as long as it is stable with respect to the electrolytic solution and has excellent liquid retention, and a porous sheet or nonwoven fabric made of polyolefin such as polypropylene or polyethylene is preferable.
- porous sheet examples include polyethylene, polypropylene, polyvinylidene fluoride, polyvinylidene chloride, polyacrylonitrile, polyacrylamide, polycarbonate, polyamide, polyimide, polytetrafluoroethylene, poly (meth) acrylic acid, and copolymers thereof. And mixtures.
- Steel materials such as aluminum, stainless steel, nickel steel and copper steel can be used for the positive electrode current collector, and copper, nickel, stainless steel, nickel-plated steel, etc. can be used for the negative electrode current collector.
- the shape of the nonaqueous electrolyte secondary battery of the present invention having the above configuration is not particularly limited, and can be various shapes such as a coin shape, a cylindrical shape, a square shape, and a pouch shape.
- GC-2010 used column: DB-1 or DB-5) manufactured by Shimadzu Corporation was used for gas chromatography measurement, and Unity INOVA 500SW manufactured by Varian was used for NMR measurement.
- the organic phase was separated and washed with 100 mL of 5% aqueous sodium bicarbonate to obtain a crude product of colorless and clear liquid ethylene bis (3,3,3-trifluoropropionate).
- the yield was 24.3 g and the yield was 85%.
- the gas chromatography area of ethylenebis (3,3,3-trifluoropropionate) was 97.2%.
- the crude product was purified by reduced pressure precision distillation (sneader 5 sphere, 0.25 kPa, fraction 80 ° C.) to obtain colorless and clear liquid ethylene bis (3,3,3-trifluoropropionate).
- the gas chromatographic area of the obtained fraction was 98.7%.
- the organic phase was separated and washed with 100 mL of 5% aqueous sodium bicarbonate to obtain a crude product of tetramethylene bis (3,3,3-trifluoropropionate) as a light brown liquid.
- the yield was 23.4 g and the yield was 84%.
- the gas chromatography area of tetramethylenebis (3,3,3-trifluoropropionate) was 97.3% as measured by gas chromatography.
- the crude product was purified by vacuum distillation (sneader 5 sphere, 0.3 kPa, fraction 116 ° C.) to obtain colorless and clear liquid tetramethylene bis (3,3,3-trifluoropropionate).
- the gas chromatographic area of the obtained fraction was 99.8%.
- a non-aqueous solvent is prepared by mixing 97 wt% of propylene carbonate (PC) with ethylene bis (3,3,3-trifluoropropionate) represented by Formula 2 manufactured in Preparation Example 1 so as to be 3 wt%. did.
- this non-aqueous solvent lithium hexafluorophosphate LiPF 6 as an electrolyte was dissolved at a rate of 1 mol / L to prepare a non-aqueous electrolyte.
- a three-electrode test cell shown in FIG. 1 was produced.
- a sealed three-electrode cell manufactured by Keihin Rika Kogyo Co., Ltd. was used, and a natural graphite-coated electrode sheet (negative electrode single layer) manufactured by Piotrek Co. was cut to a predetermined size on the working electrode 1.
- a lithium metal was used for each of the counter electrode 2 and the reference electrode 3, and a separator 4 was interposed between these electrodes and immersed in the non-aqueous electrolyte 5.
- Example 2 A mixture of 97 wt% of propylene carbonate (PC) with tetramethylene bis (3,3,3-trifluoropropionate) represented by Formula 3 manufactured in Preparation Example 2 so as to be 3 wt%, and a non-aqueous solvent was added. Prepared. In this non-aqueous solvent, lithium hexafluorophosphate LiPF 6 as an electrolyte was dissolved at a rate of 1 mol / L to prepare a non-aqueous electrolyte. Using this nonaqueous electrolytic solution, a three-electrode test cell shown in FIG. 1 was produced.
- PC propylene carbonate
- tetramethylene bis (3,3,3-trifluoropropionate) represented by Formula 3 manufactured in Preparation Example 2 so as to be 3 wt%, and a non-aqueous solvent was added.
- LiPF 6 lithium hexafluorophosphate LiPF 6 as an electrolyte was dissolved at
- Example 1 A three-electrode test cell shown in FIG. 1 was prepared in the same manner as in Examples 1 and 2 except that 100 wt% of propylene carbonate (PC) was used as the non-aqueous solvent.
- PC propylene carbonate
- a 2032 type coin cell non-aqueous electrolyte secondary battery shown in FIG. 5 was prepared using an electrolyte containing ethylene bis (3,3,3-trifluoropropionate) (formula 2).
- a positive electrode material was prepared by mixing 93 wt% of LiCoO 2 as a positive electrode active material, 4 wt% of acetylene black as a conductive material, and 3 wt% of polyvinylidene fluoride (PVDF) as a binder.
- This positive electrode material was dispersed in N-methyl-2-pyrrolidone (NMP) to form a slurry. This slurry was applied to one side of a positive electrode current collector made of aluminum, dried, and press-molded to produce a LiCoO 2 positive electrode.
- NMP N-methyl-2-pyrrolidone
- LiNi 1/3 Mn 1/3 Co 1/3 O 2 92 wt% as a positive electrode active material, 5 wt% of acetylene black as a conductive material, and 3 wt% of polyvinylidene fluoride (PVDF) as a binder are mixed, did.
- This positive electrode material was dispersed in N-methyl-2-pyrrolidone (NMP) to form a slurry. This slurry was applied to one side of a positive electrode current collector made of aluminum, dried, and press-molded to prepare a LiNi 1/3 Mn 1/3 Co 1/3 O 2 positive electrode.
- NMP N-methyl-2-pyrrolidone
- a 2032 type coin cell member made of SUS316L is used, and a LiCoO 2 positive electrode or LiNi 1/3 Mn 1/3 Co 1/3 O 2 positive electrode is used as the positive electrode 6 and a graphite negative electrode is used as the negative electrode 7 respectively. What was cut into the size of was used. Between these electrodes, a polypropylene separator 9 having a thickness of 25 ⁇ m impregnated with a nonaqueous electrolytic solution 8 containing ethylenebis (3,3,3-trifluoropropionate) represented by Formula 2 in Production Example 1 is provided. Hold in the case 10 with the gasket 12 between them, and the spacer 13 and the web washer 14 are overlapped, and the cap 11 is put on, sealed and sealed to produce a 2032 type coin cell non-aqueous electrolyte secondary battery. did.
- lithium hexafluorophosphate LiPF 6 as an electrolyte was dissolved at a rate of 1.1 mol / L to prepare a non-aqueous electrolyte.
- LiPF 6 lithium hexafluorophosphate
- LiCoO 2 positive electrode a 2032 type coin cell non-aqueous electrolyte secondary battery shown in FIG. 5 was produced.
- a non-aqueous electrolyte secondary battery was produced in the same manner as in Example 3 except that the mixed solvent mixed in (1) was used.
- a mixed solvent (EC-EMC) obtained by mixing ethylene carbonate (EC) and ethyl methyl carbonate (EMC) in a volume ratio of EC: EMC 3: 7 as a non-aqueous solvent and lithium hexafluorophosphate LiPF as an electrolyte 6 was dissolved at a rate of 1.1 mol / L to prepare a non-aqueous electrolyte.
- EC-EMC ethylene carbonate
- EMC ethyl methyl carbonate
- Lithium hexafluorophosphate as an electrolyte in a non-aqueous solvent obtained by mixing ethylenebis (3,3,3-trifluoropropionate) (EBFP) (formula 2) in a volume ratio of EC-EMC: EBFP 99: 1 LiPF 6 was dissolved at a rate of 1.1 mol / L to prepare a non-aqueous electrolyte.
- EBFP ethylenebis (3,3,3-trifluoropropionate
- the nonaqueous electrolyte secondary batteries of Examples 3 to 4, Reference Examples 3 to 4, and Comparative Examples 2 and 5 produced as described above were each 4.35 V at a constant current of 3.5 mA at 25 ° C.
- the battery was further charged at a constant voltage of 4.35 V until the current value reached 0.35 mA. Then, it discharged until it became 2.75V with the constant current of 3.5 mA, and the initial stage discharge capacity was measured. Thereafter, a charge / discharge test up to 300 cycles is performed under the above charge / discharge conditions.
- the discharge capacity at 100 cycles, 200 cycles, and 300 cycles is set as the initial discharge capacity of each nonaqueous electrolyte secondary battery as 100.
- the cycle capacity retention rate was calculated as shown in Table 1 below.
- Example 3 containing ethylenebis (3,3,3-trifluoropropionate) (EBFP) (formula 2) and 4-fluoroethylene carbonate (FEC) as a non-aqueous solvent and
- EBFP ethylenebis (3,3,3-trifluoropropionate)
- FEC 4-fluoroethylene carbonate
- Examples 3 and 4 have an improved capacity retention rate per cycle, and ethylene bis (3,3,3-trifluoropropyl By containing together (Pionate) (EBFP) (Formula 2) and 4-fluoroethylene carbonate (FEC), the effect of 4-fluoroethylene carbonate (FEC) as a polymer film forming additive is improved. I understand that.
- the above fluorinated solvent 4-fluoroethylene carbonate (FEC) has an effect as a polymer film forming additive, has a high dielectric constant, and excellent oxidation resistance. It is promising as a non-aqueous solvent for batteries.
- ethylenebis (3,3,3-trifluoropropionate) (EBFP) (formula 2) improved in the effect of 4-fluoroethylene carbonate (FEC) as a polymer film forming additive
- EBFP ethylenebis (3,3,3-trifluoropropionate)
- Example 5 4-fluoroethylene carbonate (FEC), ethyl methyl carbonate (EMC), and ethylene bis (3,3,3-trifluoropropionate) (EBFP) (Formula 2) of Production Example 1 as a polymer film forming additive
- FEC fluoroethylene carbonate
- EMC ethyl methyl carbonate
- EBFP ethylene bis (3,3,3-trifluoropropionate)
- FEC ethyl methyl carbonate
- EBFP ethylene bis (3,3,3-trifluoropropionate)
- FEC fluoroethylene carbonate
- EMC ethyl methyl carbonate
- TBFP tetramethylene bis (3,3,3-trifluoropropionate)
- Example 8 4-fluoroethylene carbonate (FEC), ethyl methyl carbonate (EMC), and tetramethylene bis (3,3,3-trifluoropropionate) (TBFP) of Production Example 2 as a polymer film-forming additive (Formula 3 )
- FEC fluoroethylene carbonate
- EMC ethyl methyl carbonate
- TBFP tetramethylene bis (3,3,3-trifluoropropionate)
- FEC 4-fluoroethylene carbonate
- EMC ethyl methyl carbonate
- the non-aqueous electrolyte secondary batteries of Examples 5 to 8 and Comparative Examples 6 to 7 prepared as described above were charged to 4.5 V at a constant current of 3.5 mA at 25 ° C., respectively.
- the battery was charged at a constant voltage until the current value reached 0.35 mA at a constant voltage of 0.5 V. Then, it discharged until it became 2.75V with the constant current of 3.5 mA, and the initial stage discharge capacity of each nonaqueous electrolyte secondary battery was measured. Thereafter, a charge / discharge test up to 200 cycles was performed under the above charge / discharge conditions.
- the discharge capacities at 50 cycles, 100 cycles, and 200 cycles, respectively, and the initial discharge capacities of each non-aqueous electrolyte secondary battery were set to 100.
- the cycle capacity retention rate was calculated as shown in Table 2 below.
- EBFP ethylene bis (3,3,3-trifluoropropionate)
- TBFP tetramethylene bis (3,3,3) which is an ester represented by formula 1 as a polymer film forming additive -Trifluoropropionate)
- EBFP ethylene bis (3,3,3-trifluoropropionate)
- TBFP tetramethylene bis (3,3,3) which is an ester represented by formula 1 as a polymer film forming additive -Trifluoropropionate)
- VC vinylene carbonate
- the ester represented by the formula 1 has an effect as a polymer film forming additive for forming a polymer film on the negative electrode.
- the polymer film formed on the negative electrode by reductive decomposition of 4-fluoroethylene carbonate (FEC) by adding the ester represented by the above formula 1 together with 4-fluoroethylene carbonate (FEC) to the non-aqueous electrolyte to improve battery characteristics such as cycle capacity retention rate.
- ester represented by the above formula 1 is superior in oxidation resistance to vinylene carbonate (VC), it is used in combination with 4-fluoroethylene carbonate (FEC), which is also excellent in oxidation resistance, and added to the non-aqueous electrolyte.
- FEC 4-fluoroethylene carbonate
- Example 9 In this evaluation test, a non-aqueous electrolyte solution containing 4-fluoroethylene carbonate (FEC) was used to fabricate and charge an aluminum laminate type non-aqueous electrolyte secondary battery. Next, the charged electrode was taken out, washed and dried, then sealed in a bag of non-aqueous solvent and aluminum laminate, and stored at 85 ° C. for 4 days to evaluate the amount of gas generated.
- FEC 4-fluoroethylene carbonate
- LiNi 1/3 Mn 1/3 Co 1/3 O 2 was used for the positive electrode, and graphite was used for the negative electrode.
- a LiNi 1/3 Mn 1/3 Co 1/3 O 2 positive electrode was cut into a size of 50 mm ⁇ 50 mm, and an aluminum tab with a sealant was ultrasonically welded.
- the graphite negative electrode was cut into a size of 50 mm ⁇ 50 mm, and a nickel tab with a sealant was ultrasonically welded.
- FEC 4-fluoroethylene carbonate
- EMC ethyl methyl carbonate
- LiPF 6 lithium hexafluorophosphate LiPF 6 as an electrolyte was dissolved at a rate of 1 mol / L.
- a polyethylene separator was interposed between the positive electrode and the negative electrode, and the electrodes were fixed and integrated with a tape to prepare an electrode group.
- the electrode group was vacuum dried at 85 ° C. for 1 hour.
- the electrode group was accommodated in a cylindrical aluminum laminated bag having both ends opened.
- the prepared electrolyte solution was dripped inside the aluminum laminate bag from the other opening. After deaeration of the aluminum laminate bag, the other opening was sealed by welding to produce an aluminum laminate battery.
- the aluminum laminate type secondary battery manufactured as described above is charged at a constant current of 10 mA at 25 ° C. until it reaches 4.4 V, and further charged at a constant voltage of 4.4 V until the current value becomes 1 mA. It was. Thereafter, the battery was discharged at a constant current of 10 mA until it reached 2.70 V, and then charged again at 25 ° C. until it reached 4.4 V at a constant current of 10 mA, and further shifted to a constant voltage charge of 4.4 V. Hold at this voltage for hours.
- the positive electrode was taken out from the battery that had been charged at a constant voltage for 12 hours, and washed twice with 10 ml of dimethyl carbonate. Then, the positive electrode was dried under reduced pressure to remove dimethyl carbonate. The dried positive electrode was put in an aluminum laminate bag sealed on three sides. From the opening of the aluminum laminate bag, as a non-aqueous solvent, 4-fluoroethylene carbonate (FEC) and ethylenebis (3,3,3-trifluoropropionate) (EBFP) (formula 2) 3 wt% were mixed. 2.5 mL of an aqueous solvent was added dropwise to seal the opening.
- FEC 4-fluoroethylene carbonate
- EBFP ethylenebis (3,3,3-trifluoropropionate
- the negative electrode was taken out from the battery and washed twice with 10 ml of dimethyl carbonate. Then, the negative electrode was dried under reduced pressure to remove dimethyl carbonate. The dried negative electrode was put in an aluminum laminate bag sealed on three sides. From the opening of the aluminum laminate bag, a non-aqueous solvent in which 3 wt% of ethylenebis (3,3,3-trifluoropropionate) (EBFP) (formula 2) is mixed with 4-fluoroethylene carbonate (FEC) is added. 5 mL was dropped and the opening was sealed.
- EBFP ethylenebis (3,3,3-trifluoropropionate)
- FEC 4-fluoroethylene carbonate
- non-aqueous solvent containing 4-fluoroethylene carbonate (FEC) and ethylene bis (3,3,3-trifluoropropionate) (EBFP) (formula 2) is LiNi 1/3 in the charged state of Example 9. It was also confirmed that the amount of gas generated in the storage test with the Mn 1/3 Co 1/3 O 2 positive electrode was the same as that of 4-fluoroethylene carbonate (FEC) in Comparative Example 8, and did not promote gas generation on the positive electrode side. did it.
- the ester represented by the above formula 1 is preferable from the viewpoint of improving the oxidation resistance of the non-aqueous electrolyte under high voltage conditions, and 4-fluoroethylene carbonate (FEC) as a high dielectric constant solvent and a low viscosity solvent as Evaluation for clarifying that the non-aqueous electrolyte using the fluorinated carboxylic acid ester has the effect of modifying the polymer film was also conducted.
- FEC 4-fluoroethylene carbonate
- a non-aqueous electrolyte was prepared by dissolving, and a non-aqueous electrolyte secondary battery of a 2032 type coin cell shown in FIG. 5 was prepared using a LiCoO 2 positive electrode as the positive electrode.
- the produced non-aqueous electrolyte secondary batteries of Examples 10 to 11 and Comparative Examples 9 to 10 were charged at a constant current of 3.5 mA at 25 ° C. until reaching 4.35 V, respectively, and further regulated to 4.35 V.
- the battery was charged at a constant voltage until the current value became 0.35 mA. Then, it discharged until it became 2.75V with the constant current of 3.5 mA, and the initial stage discharge capacity of each nonaqueous electrolyte secondary battery was measured. Then, assuming that the initial discharge capacity in the nonaqueous electrolyte secondary battery of Comparative Example 9 was 100, the initial discharge capacity of each nonaqueous electrolyte secondary battery was calculated, and the results are shown in Table 4 below.
- each of the nonaqueous electrolyte secondary batteries of Examples 10 to 11 and Comparative Examples 9 to 10 was charged to 4.35 V at a constant current of 3.5 mA at 25 ° C.
- the battery was charged at a constant voltage at a constant voltage of .35 V until the current value became 0.35 mA, and then discharged at a constant current of 3.5 mA until it reached 2.75 V, and the discharge capacity D 1 before storage was measured.
- each of the non-aqueous electrolyte secondary batteries is charged at 25 ° C. with a constant current of 3.5 mA until it reaches 4.35 V, and further with a constant voltage of 4.35 V, the current value becomes 0.35 mA.
- the nonaqueous electrolyte secondary battery was stored in a thermostat bath at 60 ° C. for 10 days in this state.
- Each non-aqueous electrolyte secondary battery after storage was discharged at 25 ° C. at a constant current of 3.5 mA until it reached 2.75 V, and the discharge capacity D 2 after storage was measured.
- each of the above non-aqueous electrolyte secondary batteries is charged at 25 ° C. with a constant current of 3.5 mA until it reaches 4.35 V, and further with a constant voltage of 4.35 V, the current value becomes 0.35 mA.
- the battery was charged at a constant voltage until Thereafter, it was measured the return capacity D 3 after storage by discharging until 2.75V with a constant current of 3.5mA.
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Abstract
Description
[1]下記式1:
[2]前記両末端に3,3,3-トリフルオロプロピオネート基を有するエステルが、下記式2:
[3]前記両末端に3,3,3-トリフルオロプロピオネート基を有するエステルは、非水系溶媒全体に対して0.01~5vol%の範囲で含まれることを特徴とする[1]に記載の二次電池用非水電解液。
[4]前記4-フルオロエチレンカーボネート(FEC)又はその誘導体であるフッ素化環状カーボネートは、非水系溶媒全体に対して0.1~30vol%の範囲で含まれることを特徴とする[1]に記載の二次電池用非水電解液。
[5]前記フッ素化鎖状カルボン酸エステルは、3,3,3,-トリフルオロプロピオン酸メチルCF3CH2COOCH3、酢酸2,2,2-トリフルオロエチルCH3COOCH2CF3及びこれらの混合物から選択される少なくとも1種であることを特徴とする[1]に記載の二次電池用非水電解液。
[6]リチウムを吸蔵し且つ放出することが可能な負極及び正極、並びに[1]~[5]のいずれか1項に記載の二次電池用非水電解液を含むことを特徴とする非水電解液二次電池。
<式2で示されるエチレンビス(3,3,3-トリフルオロプロピオネート)の合成>
分留器を取り付けた50mL反応装置内で、エチレングリコール6.10g(98.3mmol)と3,3,3-トリフルオロプロピオン酸28.2g(220mmol)とを混合した。この混合物に、95%硫酸0.21g(2.1mmol)を加えて、減圧(30kPa)下、反応装置内の温度を100℃に加熱し、水を留去しながら反応させた。7時間反応後、室温まで冷却し、反応生成物に水50mLを加えて撹拌した。有機相を分け取り、5%重曹水100mLで洗浄して、無色澄明液体のエチレンビス(3,3,3-トリフルオロプロピオネート)の粗生成物を得た。収量は24.3g、収率は85%であった。ガスクロマトグラフィーにより測定したところ、エチレンビス(3,3,3-トリフルオロプロピオネート)のガスクロマトグラフィー面積は、97.2%であった。粗生成物を減圧精密蒸留(スニーダー5球,0.25kPa,留分80℃)によって精製し、無色澄明液体のエチレンビス(3,3,3-トリフルオロプロピオネート)を得た。得られた留分のガスクロマトグラフフィー面積は98.7%であった。
[スペクトルデータ]
エチレンビス(3,3,3-トリフルオロプロピオネート)
1H-NMRスペクトル(500MHz,CDCl3) δ(ppm):3.22(4H,q,J=10Hz)、4.42 (4H,s)
19F-NMRスペクトル(470MHz,CDCl3) δ(ppm):-64.0(6F,t,J=10Hz)
<式3で示されるテトラメチレンビス(3,3,3-トリフルオロプロピオネート)の合成>
分留器を取り付けた50mL反応装置内で、1,4-ブタンジオール8.11g(90.0mmol)と3,3,3-トリフルオロプロピオン酸23.9g(187mmol)とを混合した。この混合物に、95%硫酸0.16g(1.7mmol)を加えて、減圧(40kPa)下、反応装置内の温度を120℃に加熱し、水を留去しながら反応させた。8時間反応後、室温まで冷却し、反応生成物に水50mLを加えて撹拌した。有機相を分け取り、5%重曹水100mLで洗浄して、淡褐色液体のテトラメチレンビス(3,3,3-トリフルオロプロピオネート)の粗生成物を得た。収量は23.4g、収率は84%であった。ガスクロマトグラフィーにより測定したところ、テトラメチレンビス(3,3,3-トリフルオロプロピオネート)のガスクロマトグラフィー面積は、97.3%であった。粗生成物を減圧精密蒸留(スニーダー5球,0.3kPa,留分116℃)によって精製し、無色澄明液体のテトラメチレンビス(3,3,3-トリフルオロプロピオネート)を得た。得られた留分のガスクロマトグラフフィー面積は99.8%であった。
[スペクトルデータ]
テトラメチレンビス(3,3,3-トリフルオロプロピオネート)
1H-NMRスペクトル(500MHz,CDCl3) δ(ppm):1.76(4H,h,J=2.8Hz)、3.19(4H,q,J=10Hz)、4.22(4H,t,J=5.5Hz)
19F-NMRスペクトル(470MHz,CDCl3) δ(ppm):-63.9(6F,t,J=10Hz)
プロピレンカーボネート(PC)97wt%に、製造例1で製造した式2で示されるエチレンビス(3,3,3-トリフルオロプロピオネート)を3wt%となるように混合して、非水系溶媒を調製した。この非水系溶媒に、電解質としてヘキサフルオロリン酸リチウムLiPF6を1mol/Lの割合で溶解させて、非水電解液を調製した。この非水電解液を用いて、図1に示す3電極式試験セルを作製した。
プロピレンカーボネート(PC)97wt%に、製造例2で製造した式3で示されるテトラメチレンビス(3,3,3-トリフルオロプロピオネート)を3wt%となるように混合して、非水系溶媒を調製した。この非水系溶媒に、電解質としてヘキサフルオロリン酸リチウムLiPF6を1mol/Lの割合で溶解させて、非水電解液を調製した。この非水電解液を用いて、図1に示す3電極式試験セルを作製した。
非水系溶媒としてプロピレンカーボネート(PC)100wt%を用いた以外は実施例1及び2と同様にして、図1に示す3電極式試験セルを作製した。
次に、実施例1~2の結果から、負極への重合皮膜形成能が確認された製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(式2)を含む非水電解液を用いた非水電解液二次電池について、添加効果を確認するための評価試験を実施した。
[LiCoO2正極の作成]
正極活物質としてLiCoO2 93wt%、導電材としてアセチレンブラック 4wt%、及び結着剤としてポリフッ化ビニリデン(PVDF)3wt%を混合して、正極材料とした。この正極材料をN-メチル-2-ピロリドン(NMP)に分散させてスラリー状とした。このスラリーをアルミニウム製の正極集電体の片面に塗布し、乾燥後、プレス成型してLiCoO2正極を作製した。
正極活物質としてLiNi1/3Mn1/3Co1/3O2 92wt%、導電材としてアセチレンブラック 5wt%、及び結着剤としてポリフッ化ビニリデン(PVDF)3wt%を混合して、正極材料とした。この正極材料をN-メチル-2-ピロリドン(NMP)に分散させてスラリー状とした。このスラリーをアルミニウム製の正極集電体の片面に塗布し、乾燥後、プレス成型してLiNi1/3Mn1/3Co1/3O2正極を作製した。
負極活物質として人造黒鉛97wt%、結着材としてスチレンブタジエンゴム(SBR)2wt%、及びカルボキシメチルセルロース(CMC)1wt%を混合して、負極材料とした。この負極材料を水に分散させてスラリー状とした。このスラリーを銅製の負極集電体の片面に塗布し、乾燥後、プレス成型して黒鉛負極を作成した。
上記の2032型コインセルにおいては、SUS316L製の2032型コインセル部材を使用し、正極6にLiCoO2正極又はLiNi1/3Mn1/3Co1/3O2正極、負極7に黒鉛負極をそれぞれ所定の大きさに切断したものを用いた。これらの電極の間に、製造例1の式2で示されるエチレンビス(3,3,3-トリフルオロプロピオネート)を含む非水電解液8を含浸させた厚さ25μmのポリプロピレン製セパレーター9をはさんで、ガスケット12を付したケース10内に保持し、スペーサー13とウェブワッシャー14を重ね、キャップ11を被せて、密閉、封止して2032型コインセルの非水電解液二次電池を作製した。
非水系溶媒としてエチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(以下「EC-EMC」と略す。)を用いた。この混合溶媒(EC-EMC)と、皮膜形成添加剤としての4-フルオロエチレンカーボネート(FEC)と、製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)と、をEC-EMC:FEC:EBFP=99:0.5:0.5の体積比で混合して非水系溶媒を調製した。この非水系溶媒に、電解質としてのヘキサフルオロリン酸リチウムLiPF6を1.1mol/Lの割合で溶解させて、非水電解液を調製した。この非水電解液と、LiCoO2正極とを用い、図5に示す2032型コインセルの非水電解液二次電池を作製した。
エチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(EC-EMC)と、皮膜形成化合物としての4-フルオロエチレンカーボネート(FEC)と、製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)と、をEC-EMC:FEC:EBFP=99:0.9:0.1の体積比で混合した混合溶媒を用いた以外は、実施例3の場合と同様にして非水電解液二次電池を作製した。
非水系溶媒としてエチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(EC-EMC)を用い、電解質としてヘキサフルオロリン酸リチウムLiPF6を1.1mol/Lの割合で溶解させて、非水電解液を調製した。この非水電解液と、LiCoO2正極とを用い、図5に示す2032型コインセルの非水電解液二次電池を作製した。
非水系溶媒としてエチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(EC-EMC)を用い、この混合溶媒と製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)とをEC-EMC:EBFP=99:1の体積比で混合した非水系溶媒に、電解質としてヘキサフルオロリン酸リチウムLiPF6を1.1mol/Lの割合で溶解させて、非水電解液を調製した。この非水電解液と、LiCoO2正極とを用い、図5に示す2032型コインセルの非水電解液二次電池を作製した。
エチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(EC-EMC)と、製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)とをEC-EMC:EBFP=99.9:0.1の体積比で混合した非水系溶媒を用いた以外は、参考例3の場合と同様にして非水電解液二次電池を作製した。
エチレンカーボネート(EC)とエチルメチルカーボネート(EMC)とをEC:EMC=3:7の体積比で混合させた混合溶媒(EC-EMC)と、4-フルオロエチレンカーボネート(FEC)をEC-EMC:FEC=99:1の体積比で混合した非水系溶媒を用いた以外は、参考例3の場合と同様にして非水電解液二次電池を作製した。
実施例3~4の結果から、4-フルオロエチレンカーボネート(FEC)の重合皮膜形成添加剤としての効果を改善し、電池特性向上の効果が確認されたエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)又はテトラメチレンビス(3,3,3-トリフルオロプロピオネート)(TBFP)(式3)、及び4-フルオロエチレンカーボネート(FEC)を非水系溶媒として含む非水電解液を用いた高電圧非水電解液二次電池について、これらの添加効果を確認するための評価試験を実施した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)と、重合皮膜形成添加剤としての製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)と、をFEC:EMC:EBFP=20:79:1の体積比で混合した非水系溶媒に、電解質としてヘキサフルオロリン酸リチウムLiPF6を1mol/Lの割合で溶解させて、非水電解液を調製し、正極にLiCoO2正極を用い、図5に示す2032型コインセルの非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)と、重合皮膜形成添加剤としての製造例1のエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)とをFEC:EMC:EBFP=20.0:79.9:0.1の体積比で混合した非水系溶媒を用いた以外は、実施例5の場合と同様にして非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)と、重合皮膜形成添加剤としての製造例2のテトラメチレンビス(3,3,3-トリフルオロプロピオネート)(TBFP)(式3)とをFEC:EMC:TBFP=20:79:1の体積比で混合した非水系溶媒を用いた以外は、実施例5の場合と同様にして非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)と、重合皮膜形成添加剤としての製造例2のテトラメチレンビス(3,3,3-トリフルオロプロピオネート)(TBFP)(式3)とをFEC:EMC:TBFP=20.0:79.9:0.1の体積比で混合した非水系溶媒を用いた以外は、実施例5の場合と同様にして非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)とをFEC:EMC=20:80の体積比で混合した非水系溶媒を用いた以外は、実施例5の場合と同様にして非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、エチルメチルカーボネート(EMC)と、重合皮膜形成添加剤としてのビニレンカーボネート(VC)とをFEC:EMC:VC=20:79:1の体積比で混合した非水系溶媒を用いた以外は、実施例5の場合と同様にして非水電解液二次電池を作製した。
次に式1で示されるエステルが、4-フルオロエチレンカーボネート(FEC)の還元分解によって形成される重合皮膜を改質することで、ガス発生を抑制する効果を確認するための評価試験を実施した。
本評価試験では、4-フルオロエチレンカーボネート(FEC)を含む非水電解液を用い、アルミラミネート型の非水電解液二次電池を作製して充電した。次に、充電した電極を取り出して洗浄、乾燥した後、新たに非水系溶媒とアルミラミネートの袋に封止し、85℃4日間保存してガス発生量を評価した。
非水系溶媒として4-フルオロエチレンカーボネート(FEC)のみを滴下した以外は、実施例9の場合と同様にして発生ガス量を求めた。評価結果を表3に示す。
次に上記式1で示されるエステルが、高電圧条件での非水電解液の耐酸化性向上の面から好ましい、高誘電率溶媒としての4-フルオロエチレンカーボネート(FEC)と、低粘度溶媒としてのフッ素化カルボン酸エステルを用いた非水電解液に対しても、重合皮膜を改質する効果があることを明らかにするための評価を実施した。
4-フルオロエチレンカーボネート(FEC)と、酢酸2,2,2-トリフルオロエチルCH3COOCH2CF3(FEA)と、重合皮膜形成添加剤としてのエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)と、をFEC:FEA:EBFP=20:79:1の体積比で混合した非水系溶媒に、電解質としてヘキサフルオロリン酸リチウムLiPF6を1mol/Lの割合で溶解させて、非水電解液を調製し、正極にLiCoO2正極を用い、図5に示す2032型コインセルの非水電解液二次電池を作製した。
4-フルオロエチレンカーボネート(FEC)と、3,3,3-トリフルオロプロピオン酸メチルCF3CH2COOCH3(FMP)と、皮膜形成添加剤としてのエチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)と、をFEC:FMP:EBFP=20:79:1の体積比で混合した非水系溶媒とした以外は、実施例10の場合と同様にして非水電解液二次電池を作製した。
非水系溶媒として4-フルオロエチレンカーボネート(FEC)と、酢酸2,2,2-トリフルオロエチルCH3COOCH2CF3(FEA)と、をFEC:FEA=20:80の体積比で混合し、エチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)を添加しなかった以外は、実施例10の場合と同様にして非水電解液二次電池を作製した。
非水系溶媒として4-フルオロエチレンカーボネート(FEC)と、3,3,3,-トリフルオロプロピオン酸メチルCF3CH2COOCH3(FMP)と、をFEC:FMP=20:80の体積比で混合し、エチレンビス(3,3,3-トリフルオロプロピオネート)(EBFP)(式2)を添加しなかった以外は、実施例10の場合と同様にして非水電解液二次電池を作製した。
容量残存率(%)=(D2/D1)×100
容量復帰率(%)=(D3/D1)×100
2 対極
3 参照極
4 セパレーター
5 電解液
6 正極
6a 正極集電体
7 負極
7a 負極集電体
8 非水電解液
9 セパレーター
10 ケース
11 キャップ
12 ガスケット
13 スペーサー
14 ウェブワッシャー
Claims (6)
- 前記3,3,3-トリフルオロプロピオネート基を有するエステルは、非水系溶媒全体に対して0.01~5vol%の範囲で含まれることを特徴とする請求項1に記載の二次電池用非水電解液。
- 前記4-フルオロエチレンカーボネート(FEC)又はその誘導体であるフッ素化環状カーボネートは、非水系溶媒全体に対して0.1~30vol%の範囲で含まれることを特徴とする請求項1に記載の二次電池用非水電解液。
- 前記フッ素化鎖状カルボン酸エステルは、3,3,3-トリフルオロプロピオン酸メチルCF3CH2COOCH3、酢酸2,2,2-トリフルオロエチルCH3COOCH2CF3及びこれらの混合物から選択される少なくとも1種であることを特徴とする請求項1に記載の二次電池用非水電解液。
- リチウムを吸蔵し且つ放出することが可能な負極及び正極、並びに請求項1~5のいずれか1項に記載の二次電池用非水電解液を含むことを特徴とする非水電解液二次電池。
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US15/324,044 US20170162909A1 (en) | 2014-07-08 | 2015-05-12 | Nonaqueous electrolytic solution including ester having 3,3,3-trifluoropropionate group and nonaqueous electrolyte battery using same |
CN201580037055.2A CN106537680A (zh) | 2014-07-08 | 2015-05-12 | 包含具有3,3,3‑三氟丙酸酯基的酯的非水电解液、以及使用其的非水电解液电池 |
JP2016532476A JPWO2016006315A1 (ja) | 2014-07-08 | 2015-05-12 | 3,3,3−トリフルオロプロピオネート基を有するエステルを含む非水電解液、及びそれを用いた非水電解液電池 |
KR1020177002406A KR20170028945A (ko) | 2014-07-08 | 2015-05-12 | 3,3,3-트리플루오로프로피오네이트기를 갖는 에스테르를 포함하는 비수 전해액, 및 그것을 사용한 비수 전해액 전지 |
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JP2017208186A (ja) * | 2016-05-17 | 2017-11-24 | 株式会社Gsユアサ | 非水電解液二次電池用非水電解液及び非水電解液二次電池 |
CN111919323A (zh) * | 2018-06-01 | 2020-11-10 | 松下知识产权经营株式会社 | 二次电池 |
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CN111033869A (zh) * | 2017-11-30 | 2020-04-17 | 松下电器产业株式会社 | 非水电解质二次电池 |
CN108172902B (zh) * | 2017-12-26 | 2021-01-19 | 深圳先进技术研究院 | 丙烯酸乙酯类化合物用作电解液添加剂、电解液、基于铝负极的二次电池及其制备方法 |
CN114556658B (zh) * | 2019-10-07 | 2024-05-28 | 三菱化学株式会社 | 非水电解液及非水电解质二次电池 |
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KR20170028945A (ko) | 2017-03-14 |
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