CA3134636A1 - Carbonate solvents for non-aqueous electrolytes for metal and metal-ion batteries - Google Patents
Carbonate solvents for non-aqueous electrolytes for metal and metal-ion batteriesInfo
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- 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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- C07C255/00—Carboxylic acid nitriles
- C07C255/01—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms
- C07C255/11—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms containing cyano groups and singly-bound oxygen atoms bound to the same saturated acyclic carbon skeleton
- C07C255/14—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms containing cyano groups and singly-bound oxygen atoms bound to the same saturated acyclic carbon skeleton containing cyano groups and esterified hydroxy groups bound to the carbon skeleton
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- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/02—Silicon compounds
- C07F7/08—Compounds having one or more C—Si linkages
- C07F7/18—Compounds having one or more C—Si linkages as well as one or more C—O—Si linkages
- C07F7/1804—Compounds having Si-O-C linkages
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- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
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- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/54—Electrolytes
- H01G11/58—Liquid electrolytes
- H01G11/62—Liquid electrolytes characterised by the solute, e.g. salts, anions or cations therein
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/54—Electrolytes
- H01G11/58—Liquid electrolytes
- H01G11/64—Liquid electrolytes characterised by additives
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- 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
- H01M10/05—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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- 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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- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/054—Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
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- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0025—Organic electrolyte
- H01M2300/0028—Organic electrolyte characterised by the solvent
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- H01M2300/0088—Composites
- H01M2300/0091—Composites in the form of mixtures
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- 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
CARBONATE SOLVENTS FOR NON-AQUEOUS ELECTROLYTES FOR METAL AND METAL-ION
BATTERIES
FIELD OF THE INVENTION
[0001] The present invention relates to carbonate solvents for non-aqueous electrolytes for batteries. More specifically, the present invention is concerned with carbonate solvents for non-aqueous electrolytes that are characterized by their low corrosiveness against aluminum current collectors at voltages higher than 4.2 V vs. Li metal.
BACKGROUND OF THE INVENTION
[0002] New technological solutions for telecommunications and especially electrification of transportation cells have been proposed for Li and Li-ion batteries. Their aim is to provide such batteries with the highest possible energy density in order to achieve higher voltage cathodes. This, however, requires high performance electrolytes which are resistant towards oxidation at the high potentials that occur during the operation of such a system. Also, other parasitic processes can cause deterioration and malfunctioning of the system. One such parasitic process is corrosion or electrolytic dissolution of the current collectors, which typically becomes significant at potentials beyond 4 V.
However, it also has some disadvantages, most notably sensitivity to moisture, causing HF to form, which causes rapid deterioration of battery performance. Another weakness is its limited thermal stability, limited solubility in polymers and emission of toxic decomposition products. The solvents used for the preparation of conventional electrolytes are cheaply available C1-C2 dialkyl carbonates and lower cyclic carbonates, most notably ethylene carbonate and propylene carbonate.
In addition, other compounds of this class have been proposed. It has been discovered that LiTFSI produces serious anodic dissolution, erroneously called corrosion, of the aluminum current collector at voltages higher than 3.6 V. This means that the electrochemical charge that should be used for the charging of the battery is consumed for aluminum dissolution, such that the battery in fact cannot be charged. When this process occurs with a smaller rate (meaning only part of the charge is consumed by the corrosion process) the battery can be charged, but repeating the charging further dissolves the current collector. This slowly leads to diminished contact between the active electrode coating and the current collector, resulting in loss of capacity. This imposes a serious drawback for long-term operation, which entails many charges and discharges of the battery system.
was developed to overcome those problems, but its main disadvantages are its very high molecular weight, its high price and its accumulation in living organisms similar to all long chain perfluoroalkanes. On the other hand, two lighter salts have been proposed:
lithium bis(fluorosulfonyl)amide ¨ LiFSI and asymmetric lithium N-flurosulfonyl-trifluoromethanesulfonyl amide ¨
LiFTFSI. Other asymmetric bisfluorosulfonyl amides have also been suggested.
However, very high concentrations of LiPF6 are needed to effectively suppress the anodic dissolution of aluminum. In fact, due to the high concentrations, it would be more accurate to label such electrolytes as LiPF6 electrolytes, with LiFSI as an additive to the LiPF6.
Furthermore, the most problematic point of this inhibition is that edges are not protected due to the cutting of electrodes to an appropriate size. Corrosion may propagate from the edges after many cycles, thus jeopardizing the long-term operation of such cells.
SUMMARY OF THE INVENTION
1. A metal or metal-ion battery comprising:
(a) a cathode comprising an aluminum current collector and having an upper potential limit of about 4.2 V or more vs a Li-metal reference electrode, (b) an anode, (c) a separator membrane separating the anode and the cathode, and (d) a low-corrosiveness non-aqueous electrolyte in contact with the anode and the cathode, wherein the battery has an upper voltage limit of about 4.2 V or more, wherein anodic dissolution of aluminum in the aluminum current collector is suppressed during battery operation at voltages up to said upper voltage limit, and wherein the electrolyte comprises, as a solvent, a carbonate compound of formula (I):
R R
0 0 (1), wherein:
R1 represents a 03-024 alkyl, a 03-024 alkoxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol), and R2 represents a 01-024 alkyl, a 01-024 haloalkyl, a 02-024 alkoxyalkyl, a 02-024 alkyloyloxyalkyl, a 03-024 alkoxycarbonylalkyl, a 01-024 cyanoalkyl, a 01-024 thiocyanatoalkyl, a 03-024 trialkylsilyl, a 04-024 trialkylsilylalkyl, a 04-024 trialkylsilyloxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), a 04-024 w-O-alkyl oligo(propylene glycol), a 05-024 w-0-trialkylsily1 oligo(ethylene glycol), or a 06-024 w-0-trialkylsily1 oligo(propylene glycol), and a conducting salt dissolved in said solvent.
2. The battery of item 1, wherein the upper potential limit of the cathode is about 4.4 V or more, preferably about 4.6 V or more, about 4.8 V or more, about 5.0 V or more, about 5.2 V or more, about 5.4 V or more, or about 5.5 V or more, vs a Li-metal reference electrode.
3. The battery of item 1 or 2, wherein the upper voltage limit of the battery is about 4.4 V or more, preferably about 4.6 V or more, more preferably about 4.8 V or more, yet more preferably about 5.0 V or more, even more preferably about 5.2 V or more, more preferably about 5.4 V or more, or most preferably about 5.5 V or more.
4. The battery of any one of items 1 to 3, wherein R1 represents a 03-024 alkyl or a 03-024 w-O-alkyl oligo(ethylene glycol), preferably a 03-024 alkyl.
5. The battery of any one of items 1 to 4, wherein R2 represents a 01-024 alkyl, a 02-024 alkoxyalkyl, a 01-024 cyanoalkyl, a 04-024 trialkylsilyloxyalkyl, a 05-024 w-0-trialkylsily1 oligo(ethylene glycol), or a 03-024 w-O-alkyl oligo(ethylene glycol), preferably a 01-024 alkyl.
6. The battery of any one of items 1 to 5, wherein the sum of the carbon atoms in R1 and R2 is:
or more, preferably 6 or more, more preferably 7 or more, yet more preferably 8 or more, and most preferably 9 or more, and/or 24 or less, preferably 20 or less, more preferably 16 or less, yet more preferably 14 or less, even more preferably 12 or less, and most preferably 10 or less.
7. The battery of any one of items 1 to 6, wherein R2 is methyl or ethyl.
8. The battery of any one of items 1 to 7, wherein R1 and/or R2 is propyl, or isopropyl (2-propyl).
9. The battery of any one of items 1 to 8, wherein R1 and/or R2 is butyl, 2-butyl, 3-butyl, isobutyl (3-methylpropyl), or tertbutyl (2,2-dimethylethyl).
10. The battery of any one of items 1 to 9, wherein R1 and/or R2 is pentyl or one of its isomers (including 2-pentyl and 3-pentyl), 2-methylbutyl, 3-methylbutyl, 1-methyl-2-butyl, and 2-methyl-2-butyl).
11. The battery of any one of items 1 to 10, wherein R1 and/or R2 is hexyl or one of its isomers (including 2-hexyl and 3-hexyl), 2-methylpentyl, 3-methylpentyl, 4-methylpentyl, 3-methyl-2-pentyl, 4-methyl-2-pentyl, 2-methyl-2-pentyl, 2-methyl-3-pentyl, 3-methyl-3-pentyl, 3,3-dimethy1-2-butyl, 2,3-dimethy1-2-butyl, 2-ethylbutyl, and 3-ethyl-2-butyl).
12. The battery of any one of items 1 to 11, wherein R1 and/or R2 is heptyl, one of its isomers, or 2-ethylhexyl.
13. The battery of any one of items 1 to 12, wherein R1 and/or R2 is 2-methoxyethyl or 2-isopropoxyethyl.
14. The battery of any one of items 1 to 13, wherein R2 is 2-cyanoethyl.
15. The battery of any one of items 1 to 14, wherein R2 is (2-trimethylsilyloxy)ethyl.
16. The battery of any one of items 1 to 15, wherein R1 and/or R2 is 2-methoxyethyl, 2-isopropoxyethyl, or 2-(2-methoxyethoxy)ethyl.
= LiCI04;
= LiP(CN),,F6_,õ where a is an integer from 0 to 6, preferably LiPF6;
= LiB(CN)pFa_p, where 6 is an integer from 0 to 4, preferably LiBF4;
= LiP(CnF2õi)yF6_y, where n is an integer from 1 to 20, and y is an integer from 1 to 6;
= LiB(CnF2n+i )5F4z, where n is an integer from 1 to 20, and 6 is an integer from 1 to 4;
= Li2Si(CnF2n+1 )EF6-E, where n is an integer from 1 to 20, and is an integer from 0 to 6;
= lithium bisoxalato borate;
= lithium difluorooxalatoborate; or = a compound represented by one of the following general formulas:
) 0 0 0 _______ ( 0 S o 4 0 0 ,.,5 R // \\ 1-1 4 II II 4 () \,, II 05 SS, R¨S-0 N¨S¨R im¨...)¨r-, // \\
II \D3 3/ II / II 0 0 0 ri R 0 R3 0 R3 , , , , __ --/ I 3 3 ----o---S-, R R R4 R7 \R6 \R5 R6 \I:16 , R Z
, N RG
CO--./ Ft3 N\t-_)/ 3 R5VN 4 N 4 N¨N R5 NI¨\ -R N¨\R-R \GR 3 , or Nr 5 i"---R \U-7---R3 N¨N =
, , , wherein:
R3 represents: Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, Al, hydrogen, or an organic cation; and R4, R5, R6, R7, R8 represent: cyano, fluorine, chlorine, branched or linear alkyl radical with 1-24 carbon atoms, perfluorinated linear alkyl radical with 1-24 carbon atoms, aryl, heteroaryl, perfluorinated aryl, or heteroaryl;
or a derivative thereof.
= an agent that improves solid electrolyte interphase and cycling properties;
= an unsaturated carbonate that improves stability at high and low voltages, and/or = an organic solvent that diminishes viscosity and increases conductivity.
w/w, and/or at most about 20%
w/w, at most about 15% w/w, at most about 10% w/w, or at most about 7% w/w of the total weight of the electrolyte.
v/v, and/or at most about 80% v/v, at most about 50% v/v, at most about 20%
v/v, at most about 15% v/v, at most about 10% v/v, or at most about 7% v/v of the total volume of the electrolyte.
= about 5% v/v of EC, = about 10% v/v of EC, = about 15% v/v of EC, = about 20% v/v of EC, = about 30% v/v of EC, = about 20% v/v of a mixture of EC and DEC, = about 25% v/v of a mixture of EC and DEC, = about 30% v/v of a mixture of EC and DEC, = about 50% v/v of a mixture of EC and DEC, = about 70% v/v of a mixture of EC and DEC, or = about 75% v/v of a mixture of EC and DEC, wherein said mixture preferably has an EC:DEC volume ratio of from about 1:10 to about 1:1, preferably of about 3:7, all w/w% being based on the total weight of the electrolyte and all v/v% being based on the total volume of the electrolyte.
v/v, and most preferably at least about 95%, of the total volume of the electrolyte.
= a lithiated oxide of transition metal(s) such as LNO (LiNi02), LMO
(LiMn204), LiCo),Nlii_x02wherein x is from 0.1 to 0.9, LMC (LiMn0002), LiCOVIn2_,(04, NMC (LiNiNnyCoz02), or NCA
(LiNixCoyAlz02), or = a lithium compound of transition metal(s) and a complex anion, such as LFP (LiFePO4), LNP
(LiNiPO4), LMP (LiMnPO4), LOP (LiCoPO4), Li2FCoPO4; LiCociFe),NliyMnzPO4, or Li2MnSia4.
r,2 ri........ ..õ...---....., õ,..ri 0 0 (I), wherein R1 represents a 03-024 alkyl, a 03-024 alkoxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol), and R2 represents a 01-024 alkyl, a 01-024 haloalkyl, a 02-024 alkoxyalkyl, a 02-024 alkyloyloxyalkyl, a 03-024 alkoxycarbonylalkyl, a 01-024 cyanoalkyl, a 01-024 thiocyanatoalkyl, a 03-024 trialkylsilyl, a 04-024 trialkylsilylalkyl, a 04-024 trialkylsilyloxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), a 04-024 w-O-alkyl oligo(propylene glycol), a 05-024 w-O-sily1 oligo(ethylene glycol), or a 06-024 w-O-sily1 oligo(propylene glycol), with proviso that when R2 is a 01-09 alkyl, R1 represents a 010-024 alkyl, a 03-024 alkoxyalkyl, a 03-024 w-0-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol).
or more, preferably 6 or more, more preferably 7 or more, yet more preferably 8 or more, and most preferably 9 or more, and/or 24 or less, preferably 20 or less, more preferably 16 or less, yet more preferably 14 or less, even more preferably 12 or less, and most preferably 10 or less.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] In the appended drawings:
Fig. 1 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, 1h at each step, in a conventional electrolyte comprising LIFSI and EC/DEC;
Fig. 2 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, 1h at each step, in a conventional electrolyte comprising LI FTFSI and EC/DEC;
Fig. 3 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, lh at each step, in a conventional electrolyte comprising LITFSI and EC/DEC;
Fig. 4 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, 1h at each step, in an electrolyte according to an embodiment of the present invention comprising LIFSI and diisobutyl carbonate;
Fig. 5 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, 1h at each step, in an electrolyte according to an embodiment of the present invention comprising LIFTFSI and diisobutyl carbonate;
Fig. 6 shows the chronoamperometry of an aluminum current collector versus Li metal at potentials increasing from 4 to 5.5 V by 0.1 V steps, 1h at each step, in an electrolyte according to an embodiment of the present invention comprising LITFSI and diisobutyl carbonate;
Fig. 7 shows the charge/discharge curves of an LCO cathode versus Li metal in a conventional electrolyte comprising LIFSI and EC/DEC;
Fig. 8 shows the charge/discharge curves of an LCO cathode versus Li metal in an electrolyte according to an embodiment of the present invention comprising LIFSI and diisobutyl carbonate;
Fig. 9 shows the charge/discharge curves of an LCO cathode versus Li metal in an electrolyte according to an embodiment of the present invention comprising LIFSI and diisobutyl carbonate + EC;
Fig. 10 shows the charge/discharge curves of an LMN cathode versus Li metal in a conventional electrolyte comprising LIFSI and EC/DEC;
Fig. 11 shows the charge/discharge curves of an LMN cathode versus Li metal in an electrolyte according to an embodiment of the present invention comprising LI FSI and diisobutyl carbonate;
Fig. 12 shows the discharge capacity of three cells versus cycle number, the first cell using LiFSI in diisobutyl carbonate, the second cell using Li FSI in 90% diisobutyl carbonate/10 % EC, and the third cell using a conventional electrolyte of 1 M LiPF6 in EC/DEC (3:7 vol).
DETAILED DESCRIPTION OF THE INVENTION
[0018] The present inventors have found that carbonate compounds of formula (I) can advantageously be used as solvents in non-aqueous electrolytes in batteries comprising a one cathode comprising an aluminum current collector because they are characterized by their low corrosiveness against aluminum, even at voltages of or higher than 4.2 V, even in electrolytes containing lithium sulfonylamide salts.
Utilization of these lithium sulfonylamide salts with conventional solvents in such high voltage systems is typically not possible as anodic dissolution of aluminum becomes the preferred electrochemical reaction and the vast majority of the charge is consumed for this detrimental corrosion process.
[0019] While the low corrosiveness of the carbonate compounds of formula (I) is especially advantageous when lithium sulfonylamide salts are the main conducting salt, the person skilled in the art would recognize the potential of these solvents for achieving high voltage lithium and lithium ion batteries in connection with other conducting salts. The skilled person would also understand that the electrolyte can be used in different types of batteries, such as sodium, potassium, calcium, aluminum and magnesium-based batteries, and that when doing so, other salts can be dissolved in the solvents, for example sodium, potassium, calcium, aluminum and magnesium salts.
[0020] Indeed, the carbonate compounds of formula (I) are characterized by their capacity to suppress anodic dissolution of aluminum (e.g. in an aluminum current collector as well as any other aluminum member in the battery) when used as solvents in electrolytes in batteries, even at potentials higher than 4.2 V, as measured vs a lithium metal reference electrode. Such examples of batteries are a lithium or lithium-ion batteries. For clarity, unless specified otherwise, all electrode potentials in the present application are referenced to a Li metal anode.
[0021] Anodic dissolution of the aluminum current collector is defined as the dissolution of an aluminum current collector at a certain externally forced potential (the critical potential), which is higher than the open circuit potential.
At the critical potential, the components of the electrolyte react with the surface of the collector and form soluble compounds, which in turn dissolve in the electrolyte and cause dissolution of the aluminum i.e. quasi corrosion.
Significant dissolution of the aluminum can lead to malfunctioning of the battery system, if its operating voltage surpasses the critical potential. Accordingly, suppressing anodic dissolution enables safer and more powerful battery technologies, especially lithium-ion batteries. Herein, "suppressing"
anodic dissolution means that anodic dissolution does not occur or that is reduced to such a level that it becomes non-deleterious to the battery.
[0022] This low corrosiveness of the carbonate compounds of formula (I) also enables the manufacture of batteries containing aluminum current collectors with extended operating voltages (in particular, operating voltages over 4.2 V vs a Li-metal reference electrode), even for electrolytes containing lithium sulfonylamide salts and lithium-ion batteries. This allows for the preparation of non-aqueous electrolytes containing lithium sulfonylamide salts that are free of corrosion inhibitors (while still maintaining said low corrosiveness against aluminum current collectors at voltages higher than 4.2 V).
[0023] Furthermore, when compared to conventional carbonate solvents (e.g.
ethylene carbonate (EC), diethyl carbonate (DEC), and the like), the carbonate compounds of formula (I) have a wider operating temperature range, especially when used in lithium-ion batteries. Indeed, the temperature range in which the carbonate compounds of formula (I) are liquid (without crystallization) tends to be wider than that of these conventional carbonate solvents.
For example, in embodiments, the carbonate compounds of formula (I) can have a melting point well below -10 C, and, in some cases, do not even have a melting point and thus stay liquid, without crystallizing, until they reach their glass transition point. Further, the melting point of the carbonate compounds tends to decrease with growing molecular mass to a certain point.
[0024] Further, the carbonate compounds of formula (I) have a higher boiling point than conventional carbonate solvents. For example, the boiling points of dimethyl carbonate, diethyl carbonate, dipropyl carbonate and dibutyl carbonate are 90, 126, 168 and 207 C, respectively. This indicates that electrolytes prepared from higher carbonates can be used at higher temperatures without the risk of rapid evaporation. These higher boiling points translates into improved safety properties for the batteries containing the electrolyte using the carbonate compounds of formula (I) as solvent.
[0025] Finally, the carbonate compounds of formula (I) are a very green, that is environmentally benign, group of solvents.
[0026] The inventors thus provide herein a metal or metal-ion battery comprising:
(a) a cathode comprising an aluminum current collector and having an upper potential limit of about 4.2 V or more vs a Li-metal reference electrode, (b) an anode, (c) a separator membrane separating the anode and the cathode, and (d) a low-corrosiveness non-aqueous electrolyte in contact with the anode and the cathode, wherein the battery has an upper voltage limit of about 4.2 V or more, wherein anodic dissolution of aluminum in the aluminum current collector is suppressed during battery operation at voltages up to said upper voltage limit, and wherein the electrolyte comprises, as a solvent, a carbonate compound of formula (I) and a conducting salt dissolved in said solvent.
[0027] In embodiments, the upper potential limit of the cathode is preferably about 4.4 V or more, about 4.6 V or more, about 4.8 V or more, about 5.0 V or more, about 5.2 V or more, about 5.4 V or more, or about 5.5 V or more, vs a Li-metal reference electrode.
[0028] In embodiments, the upper potential limit of the cathode is preferably about 6.0 V or less, about 5.6 V or less, about 5.5 V or less, about 5.4 V or less, about 5.2 V or less, about 5.0 V or less, about 4.8 V or less, vs a Li-metal reference electrode.
[0029] In embodiments, the upper voltage limit of the battery is preferably about 4.4 V or more, about 4.6 V or more, about 4.8 V or more, about 5.0 V or more, about 5.2 V or more, about 5.4 V or more, or about 5.5 V or more.
[0030] In embodiments, the upper voltage limit of the battery is preferably about 6.0 V or less, about 5.6 V or less, about 5.5 V or less, about 5.4 V or less, about 5.2 V or less, about 5.0 V or less, about 4.8 V or less.
[0031] The lower potential limit of the cathode and the lower voltage limit of the battery are not substantially affected by using a carbonate compound of formula (I) as a solvent in the battery of the invention. Indeed, these lower limits are not critical to the invention since anodic dissolution occurs only at elevated potentials. Furthermore, the lower potential limit of cathode it typically not affected by the solvent used for the electrolyte. Therefore, these lower limits will be those found in corresponding conventional batteries that use other solvents.
[0032] Indeed, cathodes are characterized by a potential window that goes from a lower potential limit to an upper potential limit. The lower potential limit is the potential beyond which further discharge would harm the cathode.
The upper potential limit is the potential beyond which further charge would harm the cathode. These potential values are always given referring to a certain reference. For example, for all lithium batteries, this reference is a Li-metal reference electrode. Herein, the potential values all refer to a Li-metal reference electrode, even when referring to other types of batteries (sodium-based, magnesium-based batteries, etc.).
[0033] Furthermore, batteries are characterized by an operating voltage window that goes from a lower voltage limit to an upper voltage limit. The lower voltage limit is the voltage at which a battery is considered fully discharged and beyond which further discharge would harm the battery (or its components).
The upper potential limit is the voltage at which a battery is considered fully charged and beyond which further charge would harm the battery (or its components). Therefore, batteries are operated at voltages within their operating voltage window, i.e. they are charged/discharged so that their voltage falls within their operating voltage window, ideally as close as possible to the upper voltage limit when they are charged so as to provide a maximum of energy.
[0034] For note, a battery voltage is the difference between the potential of the cathode and that of the anode.
Battery voltage = (potential of the cathode) ¨ (potential of the anode) As such, no reference is needed when providing a battery voltage value.
[0035] When the anode of the battery is lithium metal, it has (all the time) a potential of OV. Thus, in such cases, the upper and lower voltage limits of the battery are equal to the upper and lower potential limits of the cathode. In other cases, such as when the anode is made of graphite, the anode has a potential >OV. When the anode has a potential >0V, the upper and lower voltage limits of the battery are lower than the upper and lower potential limits of the cathode, respectively. For example, a graphite anode has (most of the time) a potential of about 0.1V, but this potential can nevertheless vary from about 2,5V to very close to OV. An LTO anode has a potential of about 1.5V most of the time.
[0036] As noted above, anodic dissolution of aluminum in the aluminum current collector is suppressed during battery operation at voltages at least up to said upper voltage limit. Herein, the "suppression" of anodic dissolution means that this phenomenon does not take place at all or that it is so limited that the battery can be charged up to said upper voltage without losing significant part of charge for anodic dissolution of aluminium. For example, less than 0.01%, preferably less than 0.001%, and more preferably less than 0.0001%
of the charge is lost. In another scale, it is preferable that the corrosion current density be lower than about 1 microA/cm2. Indeed, when significant anodic dissolution occurs within the operating voltage window of a battery, significant amount of charge is lost, and significant amount of aluminium is dissolved and contact between the current collector and active material lost, further leading into loss of useful capacity. In the most catastrophic scenario, most of the charge is consumed by aluminium dissolution when first charging the battery, which means that the amount of charge stored by the battery (i.e. the amount of useful charge) is very small. In other words, the battery does not work. In particular, electrolytes comprising bis(sulfonylamide) salts (of e.g. lithium or of other metals in batteries based on other metals) can cause such catastrophic anodic dissolution of aluminium. In contrast, when such salts are dissolved in a carbonate compound of formula (I), as a solvent, the anodic dissolution is successfully supressed.
[0037] In preferred embodiments, the battery is a lithium battery, a lithium-ion battery, sodium battery, a sodium-ion battery, a potassium battery, a potassium-ion battery, a magnesium battery, a magnesium-ion battery, an aluminum battery, or an aluminum ion battery. Preferably, the battery is a lithium battery, a lithium-ion battery, sodium battery, a sodium-ion battery, a potassium battery, a potassium-ion battery, a magnesium battery, a magnesium-ion battery. In more preferred embodiments, the battery of the present invention is a lithium battery or lithium-ion battery, even more preferably a lithium-ion battery.
[0038] More details on the various components of the battery of the invention are provided in the following sections.
[0039] There is also provided a method of manufacturing and/or operating a battery as describe above, said method comprising the step of charging the battery up to an upper voltage limit of about 4.2 V or more, preferably about 4.4 V or more, about 4.6 V or more, about 4.8 V or more, about 5.0 V or more, about 5.2 V or more, about 5.4 V or more, or about 5.5 V or more.
Carbonate compound of formula (I) [0040] The carbonate compound of formula (I) is:
0 0 (1), wherein R1 represents a 03-024 alkyl, a 03-024 alkoxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol), and R2 represents a 01-024 alkyl, a 01-024 haloalkyl, a 02-024 alkoxyalkyl, a 02-024 alkyloyloxyalkyl, a 03-024 alkoxycarbonylalkyl, a 01-024 cyanoalkyl, a 01-024 thiocyanatoalkyl, a 03-024 trialkylsilyl, a 04-024 trialkylsilylalkyl, a 04-024 trialkylsilyloxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), a 04-024 w-O-alkyl oligo(propylene glycol), a 05-024 w-0-trialkylsilyloligo(ethylene glycol), or a 06-024 w-0-trialkylsilyloligo(propylene glycol).
[0041] In more preferred embodiments, R1 represents a 03-024 alkyl or a 03-024 w-O-alkyl oligo(ethylene glycol).
In more preferred embodiments, R1 represents a 03-024 alkyl.
[0042] In more preferred embodiments, R2 represents a 01-024 alkyl, a 02-024 alkoxyalkyl, a 01-024 cyanoalkyl, a 04-024 trialkylsilyloxyalkyl, a 05-024 w-0-trialkylsily1 oligo(ethylene glycol), or a 03-024 w-O-alkyl oligo(ethylene glycol). In most preferred embodiments, R2 represents a C1-024 alkyl.
[0043] Given that R1 and R2 as defined above contain at least 3 and 1 carbon atoms, respectively, the sum of the carbon atoms in R1 and R2 is at least 4. In preferred embodiments, the sum of the carbon atoms in R1 and R2 is:
5 or more, preferably 6 or more, more preferably 7 or more, yet more preferably 8 or more, and most preferably 9 or more, and/or 24 or less, preferably 20 or less, more preferably 16 or less, yet more preferably 14 or less, even more preferably 12 or less, and most preferably 10 or less.
[0044] Each of the alkyl and substituted alkyl in R1 and R2 are linear or branched.
[0045] Herein, "alkyl" has its usual meaning in the art. Specifically, it is a monovalent saturated aliphatic hydrocarbon radical of general formula -C,1-12i-H-1.
[0046] Non-limiting examples of 03-024 alkyl in R1 include propyl, isopropyl (2-propyl), butyl, 2-butyl, 3-butyl, isobutyl (3-methylpropyl), tertbutyl (2,2-dimethylethyl), 2-methylbutyl, 3-methylbutyl, 1-methyl-2-butyl, 2-methyl-2-butyl, 2-methylpentyl, 3-methylpentyl, 4-methylpentyl, 3-methyl-2-pentyl, 4-methyl-2-pentyl, 2-methyl-2-pentyl, 2-methy1-3-pentyl, 3-methyl-3-pentyl, 3,3-dimethy1-2-butyl, 2,3-dimethy1-2-butyl, 2-ethylbutyl, 3-ethyl-2-butyl, 2-ethylhexyl, pentyl and its isomers (including 2-pentyl and 3-pentyl), hexyl and its isomers (including 2-hexyl and 3-hexyl), heptyl and its isomers, octyl and its isomers, nonyl and its isomers, decyl and its isomers, undecyl and its isomers, and dodecyl and its isomers. In preferred embodiments, the 03-024 alkyl in R1 is a 03-018 alkyl, preferably a 03-012 alkyl, preferably a 03-Gil alkyl, preferably a 03-010 alkyl, preferably a 03-09 alkyl, more preferably a 03-08 alkyl, even more preferably a 03-07 alkyl (yet more preferably a 04-07 alkyl), yet more preferably a 03-06 alkyl (yet more preferably a Ca-Cs alkyl), more preferably a 03-05 alkyl, and most preferably a Ca-Cs alkyl.
[0047] Non-limiting examples of 01-024 alkyl chain in R2 include the 03-024 alkyls listed above with regard to R1, as well as methyl and ethyl. In preferred embodiments, R2 is a 01-018 alkyl, preferably a 01-012 alkyl, a 01-09 alkyl, a 01-08 alkyl, a 01-07 alkyl, a 02-07 alkyl, a 03-07 alkyl (preferably a 04-07 alkyl), a 03-06 alkyl (preferably a Ca-Cs alkyl), a 03-05 alkyl, and most preferably a Ca-Cs alkyl.
[0048] In preferred embodiments, both R1 and R2 are alkyl groups. In more preferred embodiments, R1 and R2 are the same alkyl groups. In alternative preferred embodiments, R1 and R2 are different alkyl groups.
[0049] Preferred 03 alkyls in R1 and R2 include propyl, and isopropyl (2-propyl).
[0050] Preferred 04 alkyls in R1 and R2 include butyl, 2-butyl, 3-butyl, isobutyl (3-methylpropyl), and tertbutyl (2,2-di methylethyl).
[0051] Preferred Cs alkyls in R1 and R2 include pentyl and its isomers (including 2-pentyl and 3-pentyl), 2-methylbutyl, 3-methylbutyl, 1-methyl-2-butyl, and 2-methyl-2-butyl.
[0052] Preferred 06 alkyls in R1 and R2 include hexyl and its isomers (including 2-hexyl and 3-hexyl), 2-methylpentyl, 3-methylpentyl, 4-methylpentyl, 3-methyl-2-pentyl, 4-methyl-2-pentyl, 2-methyl-2-pentyl, 2-methy1-3-pentyl, 3-methyl-3-pentyl, 3,3-dimethy1-2-butyl, 2,3-dimethy1-2-butyl, 2-ethylbutyl, and 3-ethyl-2-butyl.
[0053] Preferred 07 alkyls in R1 and R2 include heptyl and its isomers.
[0054] Preferred 08 alkyls in R1 and R2 include 2-ethylhexyl.
[0055] Herein, a "haloalkyl" refers to an alkyl group in which one or more (or even all) of the hydrogen atoms are each replaced by a halogen atom, wherein the halogen atoms are the same or different from one another (when more than one halogen atoms are present). Halogen atoms include fluorine (F), chlorine (CI), bromine (Br), and iodine (1). Preferably, the halogen atom is fluorine. Non-limiting examples of 01-024 haloalkyls in R2 include trifluoromethyl, pentafluoroethyl, heptafluoropropyl, nonafluorobutyl, 2,2,2-trifluoroethyl, and 1,1,1,3,3,3-hexafluoro-2-propyl.
[0056] Herein, an "alkoxyalkyl" refers to an alkyl group in which one or more, preferably one, of the hydrogen atoms are each replaced by an alkoxy group, wherein the alkoxy groups are the same or different from one another (when more than one alkoxy groups are present). In preferred embodiments, the alkoxyalkyl comprises only one alkoxy group. An alkoxy group is a radical of formula -0-alkyl, this alkyl being linear or branched, preferably linear.
A 02-024 alkoxyalkyl is alkoxyalkyl radical, wherein the sum of the number of carbon atoms contained in the alkyl and alkoxy groups is between 2 and 24. In preferred embodiments, the alkoxyalkyl is a (Ci-02)alkoxy(02-06)alkyl.
Non-limiting examples of alkoxyalkyls in R2 or R1 include 2-methoxyethyl, 3-methoxypropyl, 2-methoxypropyl, 4-methoxybutyl, 4-ethoxybutyl, 5-methoxypentyl, 6-methoxyhexyl, and 2-isopropoxyethyl. In preferred embodiments, the alkoxyalkyl is 2-methoxyethyl or 2-isopropoxyethyl.
[0057] Herein, an "alkyloyloxyalkyl" refers to an alkyl group in which one or more, preferably one, of the hydrogen atoms are each replaced by an alkyloyloxy group, wherein the alkyloyloxy groups are the same or different when more than one alkyloyloxy groups are present). In preferred embodiments, the alkyloyloxyalkyl comprises only one alkyloyloxy group. An alkyloyloxy group is a radical of formula -0-C(=0)-alkyl, this alkyl being linear or branched.
A 02-024 alkyloyloxyalkyl is alkyloyloxyalkyl wherein the sum of the number of carbon atoms contained in the alkyl and alkyloyloxy groups is between 2 and 24. Non-limiting examples of 02-024 alkyloyloxyalkyl in R2 include 2-acetoxyethyl, 3-acetoxypropyl, 2-acetoxypropyl, and 4-acetoxybutyl.
[0058] Herein, an "alkoxycarbonylalkyl" refers to an alkyl group in which one or more of the hydrogen atoms are each replaced by an alkoxycarbonyl group, wherein the alkoxycarbonyl groups are the same or different from one another (when more than one alkoxycarbonyl groups are present). In preferred embodiments, the alkoxycarbonylalkyl comprises only one alkoxycarbonyl group. An alkoxycarbonyl group is a radical of formula -C(=0)-0-alkyl, this alkyl being linear or branched. A 02-024 alkoxycarbonyl is an alkoxycarbonyl wherein the sum of the number of carbon atoms contained in the alkyl and alkoxycarbonyl groups is between 3 and 24. Non-limiting examples of 03-024 alkoxycarbonylalkyl in R2 include 2-ethoxycarbonylethyl and 3-methoxycarbonylpropyl.
[0059] Herein, a "cyanoalkyl" refers to an alkyl group in which one or more of the hydrogen atoms are each replaced by a cyano (-GEN) group. In preferred embodiments, the cyanoalkyl comprises only one cyano group. In preferred embodiments, the cyanoalkyl is a 01-05 cyanoalkyl. Non-limiting examples of 01-024 cyanoalkyls in R2 include cyanomethyl, 2-cyanoethyl, 3-cyanopropyl, 4-cyanobutyl, and 5-cyanopentyl. In preferred embodiments, the 01-024 cyanoalkyl in R2 is 2-cyanoethyl.
[0060] Herein, a "thiocyanatoalkyl" refers to an alkyl group in which one or more of the hydrogen atoms are each replaced by a thiocyanato (-S-CEN) group. In preferred embodiments, the thiocyanatoalkyl comprises only one thiocyanato group. Non-limiting examples of 01-024 thiocyanatoalkyls in R2 include thiocyanatomethyl, 2-thiocyanatoethyl, 3-thiocyanatopropyl, 4-thiocyanatobutyl, 5-thiocyanatopentyl, and 6-thiocyanatohexyl.
[0061] Herein, a "trialkylsilyl" refers to a radical of formula (alky1)3-Si-, wherein the alkyl groups are the same or different and are linear or branched. A 03-024 trialkylsilyl is a trialkylsilyl wherein the sum of the number of carbon atoms contained in all of the alkyl groups is between 3 and 24. In preferred embodiments, each of the alkyl groups in the trialkylsilyl is a 01-04 alkyl group. In preferred embodiments, the three alkyl groups are the same. Non-limiting examples of 03-024 trialkylsilyls in R2 include trimethylsilyl, ethyldimethylsilyl, diethylmethylsilyl, triethylsilyl, dimethylpropylsilyl, dimethylisopropylsilyl, triisopropylsilyl, butyldimethylsilyl, and tertbutyldimethylsilyl.
[0062] Herein, a "trialkylsilylalkyl" is an alkyl group in which one or more of the hydrogen atoms are each replaced by a trialkylsilyl group, wherein the trialkylsilyl are as defined above and are the same or different from one another (when more than one trialkylsilyl groups are present). In a 04-024 trialkylsilylalkyl, the sum of the number of carbon atoms contained in all four of the alkyl groups is between 4 and 24.
Preferably, the trialkylsilylalkyl comprises only one trialkylsilyl group. In preferred embodiments, the 04-024 trialkylsilylalkyl is a trialkylsilylalkyl(Ci-04)alkyl, preferably a trialkylsilylalkyl(02-04)alkyl. In preferred embodiments, the three alkyl groups attached to the Si atom are methyl groups. Non-limiting examples of 04-024 trialkylsilylalkyl in R2 include trimethylsilylethyl, 2-trimethylsilyethyl, 3-trimethylsilylpropyl and 4-trimethylsilylbutyl.
[0063] Herein, a "trialkylsilyloxyalkyl" refers to an alkyl group in which one or more of the hydrogen atoms are each replaced by a trialkylsilyloxy group, wherein the trialkylsilyloxy groups are the same or different from one another (when more than one trialkylsilyloxy groups are present). Preferably, the trialkylsilyloxyalkyl comprises only one trialkylsilyloxy group. Herein, a "trialkylsilyloxy" is a radical of formula (alkyl)3-Si-O-, wherein the alkyl groups are the same or different from one another and are linear or branched. In a 04-024 trialkylsilyloxyalkyl, the sum of the number of carbon atoms contained in all four of the alkyl groups is between 4 and 24. In preferred embodiments, the 04-024 trialkylsilyloxyalkyl is a trialkylsilyloxy(03-04)alkyl. In preferred embodiments, the three alkyl groups attached to the Si atom are methyl groups. Non-limiting examples of 04-024 trialkylsilyloxyalkyl in R2 include (2-trimethylsilyloxy)ethyl, 3-trimethylsilyloxypropyl and 4-trimethylsilyloxybutyl. In preferred embodiments, the 04-024 trialkylsilyloxyalkyl in R2 is (2-trimethylsilyloxy)ethyl.
Preferred such compounds include those in which, when R2 is a 01-09 alkyl, R1 represents a 03-024 alkoxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol).
Non-aqueous electrolyte
Conducting Salt
For example, for an electrolyte containing less of the carbonate compound of formula (I) of the present invention, the addition of a passivating conducting salt will produce an electrolyte which nonetheless prevents anodic dissolution of aluminum. Some inorganic salts like LiPF6 passivate the surface of the aluminum, as they form insoluble compounds and thus do not cause anodic dissolution up to more than 5 V vs Li anodes. In contrast, some salts do not passivate aluminum, especially lower fluorinated sulfonyl amides, which cause a very strong dissolution of aluminum. As mentioned, this can lead to malfunctioning of the battery system if its operating voltage surpasses the critical potential. When such conducting salts are used, it is preferable to include more of the carbonate compound of formula (I) in the electrolyte so as to further prevent anodic dissolution.
LiP(C,-,F2õi)yF6_y, where n is an integer from 1 to 20, and y is an integer from 1 to 6; LiB(C,-,F2õ1 )6F4_6, where n is an integer from 1 to 20, and 6 is an integer from 1 to 4; Li2Si(C,-,F2õ1),F6, where n is an integer from 1 to 20, and is an integer from 0 to 6; lithium bisoxalato borate; lithium difluorooxalatoborate; and compounds represented by the following general formulas:
\ 0 4 0 0 S
0 0 __ K 0 S 0 R,.... // \\ ,,...R5 0 0 C) \ II ,_,5 S S, R-S-0 N-S-R N-0- ri ii .---.../ \\ --- 0 -- S ----I I \ 0 ----/4 0 , , , , , R R7 R6 ( GIR4 3 R6( \ N'G- R5 3 R(G 53 N't-------R34"-*-RR4 , R.-(c--......-R4 Nri,--...\\yõ-::)"/"---R3 \i'-' 3 N-N and N-N ; wherein R3 represents: Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, Al, hydrogen, or an organic cation; and R4, R5, R6, R7, R8 represent: cyano, fluorine, chlorine, branched or linear alkyl radical with 1-24 carbon atoms, perfluorinated linear alkyl radical with 1-24 carbon atoms, aryl or heteroaryl radical, or perfluorinated aryl or heteroaryl radical;
and their derivatives.
The concentration of the conducting salt refers to the molarity of the conducting salt in the carbonate solvent and any other solvents (if present), disregarding the presence of additives. This can be represented by the following equation:
moles of conducting salt Concentration of conducting salt ¨ __________________________ volume of the electrolyte wherein the volume of the electrolyte is the final total volume of the carbonate compound of formula (I), the dissolved salt, and any liquid additive present.
Additives that Improve the Electrochemical Properties of the Electrolyte
= agents that improve solid electrolyte interphase (SEI) and cycling properties, = unsaturated carbonates that improve stability at high and low voltages, and = organic solvents that diminish viscosity and increase conductivity.
In preferred embodiments, such organic solvents are present. Non-limiting examples of organic solvents that diminish viscosity and increase conductivity include polar solvents, preferably alkyl carbonates, alkyl ethers, and alkyl esters. For example, the organic solvent may be ethylene carbonate, propylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, dimethoxyethane, diglyme (diethylene glycol dimethyl ether), triglyme (triethylene glycol dimethyl ether), tetraglyme ((tetraethylene glycol dimethyl ether), tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxolane, 2,2-dimethy1-1,3-dioxolane, 1,4-dioxane, 1,3-dioxane, methoxypropionitril, propionitril, butyronitrile, succinonitrile, glutaronitrile, adiponitrile, esters of acetic acid, esters of propionic acid, cyclic esters like y-butyrolactone, c-caprolactone, esters of trifluoroacetic acid, sulfolane, dimethyl sulfone, ethyl methyl sulfone, or peralkylated sulfamides. In embodiments, ionic liquids could also be added in order to diminish flammability and to increase conductivity. Preferred organic solvents that diminish viscosity and increase conductivity include ethylene carbonate (EC), dimethyl carbonate (DMC), ethyl methyl carbonate (EMC) and diethyl carbonate (DEC).
of the total mass of the electrolyte. In embodiments, the amount of these additives represents a total of at least about 0.1% w/w, at least 1% w/w, at least about 2% w/w, at least about 5% w/w, or at least about 7% w/w, and/or at most about 20% w/w, at most about 15% w/w, at most about 10% w/w, or at most about 7% w/w of the total weight of the electrolyte.
v/v, at most about 10% v/v, or at most about 7% v/v of the total volume of the electrolyte.
= up to about 5% v/v of EC, = up to about 10% v/v of EC, = up to about 15% v/v of EC, = up to about 20% v/v of EC, = up to about 30% v/v of EC, = up to about 20% v/v of a mixture of EC and DEC, = up to about 25% v/v of a mixture of EC and DEC, = up to about 30% v/v of a mixture of EC and DEC, = up to about 50% v/v of a mixture of EC and DEC, = up to about 70% v/v of a mixture of EC and DEC, or = up to about 75% v/v of a mixture of EC and DEC, all w/w% being based on the total weight of the electrolyte and all v/v% being based on the total volume of the electrolyte.
Corrosion Inhibitors
of the total weight of the electrolyte. In embodiments, the total amount of corrosion inhibitors represents at least about 1% w/w, at least about 2% w/w, at least about 5% w/w, or at least about 10% w/w, and/or at most about 35%
w/w, at most about 25% w/w, at most about 20% w/w, at most about 15% w/w, at most about 10% w/w, or at most about 7% w/w of the total weight of the electrolyte.
Minimum Concentration of Compound of Formula (I) in the Electrolyte
v/v, even more preferably at least about 90% v/v, and most preferably at least about 95%, of the total volume of the electrolyte.
v/v, more preferably at least about 20%
v/v, yet more preferably at least about 25% v/v, and most preferably at least about 30%, based on the volume of the electrolyte.
Remaining Components of the Batteries
(a) a cathode comprising an aluminum current collector, (b) an anode, (c) a separator membrane separating the anode and the cathode, and (d) a low-corrosiveness non-aqueous electrolyte in contact with the anode and the cathode.
which include various forms of conductive carbon, such as carbon nanotubes and carbon black - and subsequently coated on a copper current collector in order to obtain the anode. In preferred embodiments, the anode is made of lithium metal or graphite.
(LiMn3/2Niv204), LMC (LiMn0002), LiCOVIn2õ04, NMC (LiNiNnyCoz02), NCA
(LiNixCoyAlz02), lithium compounds with transition metals and complex anions, LFP (LiFePO4), LNP (LiNiPO4), LMP
(LiMnPO4), LOP (LiCoPO4), Li2FCoPO4; LiCociFe),NliyMnzPO4, and Li2MnSiO4.
(v) porous polymeric membranes provided with an additional ceramic layer in order to improve the performance at high potentials; and (vi) polymer electrolyte membranes. However, as mentioned, the separator membrane can also be any separator membrane typically used for a battery, preferably for a lithium or a lithium ion battery; for example Celgard 35011M or Celgard Q20S1HX TM.
Method of producing the carbonate solvents, the non-aqueous electrolytes, and the batteries
0 R6ONa ,...,6 ,...,õ
H3C CH3 in¨ yr, 6 6 R /. CH3 R /\ R6 H3C¨OH
Syntheses of alkyl carbonates are very well-developed processes. While the most convenient methods are discussed below, the skilled person would understand that other synthesis methods can be used.
For this reason, the use of lower carbonates is preferred over higher carbonates because the formed alcohol has a lower boiling point; however, attention must be paid to the formation of azeotropic mixtures which may complicate the separation.
The amount of sodium should be chosen so that it will react with the water present in the reactants and consume it all. In this way, a water free solvent can be isolated. The process of sodium dissolution can be accelerated by heating and stirring, which is necessary with all higher alcohols. A protective atmosphere of nitrogen or argon should be used to exclude the uptake of carbon dioxide and water from the atmosphere. When sodium is dissolved, the starting carbonate ester is added and the mixture is refluxed at such a temperature that the alcohol which is formed during the reaction distills from the reaction mixture, while all reactants remain in the reactor.
After the reaction is finished, the components of the reaction mixture are separated by fractional distillation, under vacuum for higher alkyl carbonates. In this manner the solvents can be isolated in high purity if no azeotropes are formed.
Definitions
Further, all subsets of molecules within the general chemical structures are also incorporated into the specification as if they were individually recited herein.
= alkyloyl is alkyl-C(=0)-, = aryloyl is aryl-C(=0)-, = alkyloxycarbonyl is alkyl-O-C(=0)-, and = aryloxycarbonyl is aryl-O-C(=0)-.
LiMn3/2Ni v204,
DESCRIPTION OF ILLUSTRATIVE EMBODIMENT
Preparation of carbonate solvents of the invention Example 1: Preparation of diisobutyl carbonate (Solvent no. 10) by transesterification
Unreacted isobutanol, dimethyl carbonate and isobutyl methyl carbonate were also detected in the preceding fraction. The structure of the products was confirmed by NMR (nuclear magnetic resonance spectroscopy), IR
(infra-red spectroscopy) and GC/MS (gas chromatography with mass selective detector) analyses.
Example 2: Preparation of di(2-pentyl) carbonate (Solvent no. 17) and methyl 2-pentyl carbonate (Solvent no. 16) by transesterification
Example 3: Preparation of 2-cyanoethyl butyl carbonate (Solvent no. 23) by reaction of butyl chloroformate and 3-hydroxypropinonitril
After the addition, the mixture was stirred at room temperature for 2h, after which water and sulfuric acid were added and the mixture was separated by means of a separation funnel. The organic phase was washed 4 times with water, and then dried with anhydrous magnesium sulfate, filtered, and evaporated. Distillation of the remaining clear oil gave pure product (13.1 g). Structure of the products was confirmed by NMR, IR and GC/MS analyses.
Example 4: Preparation of other carbonate solvents of the present invention
Table 1 Solvent Name 1H NMR 13C NMR
No (400MHz, CHLOROFORM-d) 6 = (101MHz, CHLOROFORM-d) 6=
1 didodecyl carbonate 4.10 (t, J=6.8 Hz, 2H), 1.65 (br quin, 155.39, 67.92, 31.88, 29.61, J=6.8 Hz, 2H), 1.40- 1.22 (m, 18H), 29.59, 29.53, 29.46, 29.32, 29.21, 0.87 (br t, J=6.8 Hz, 3H) 28.67, 25.68, 22.64, 14.03 2 dibutyl carbonate (400MHz, DICHLOROMETHANE-d2) 6 (101MHz, = 4.07 (t, J=6.7 Hz, 1H), 1.60 (br quin, DICHLOROMETHANE-d2) 6 =
J=7.3 Hz, 1H), 1.37 (br sxt, J=7.5 Hz, 156.02, 68.06, 31.45, 19.62, 1H), 0.91 (t, J=7.4 Hz, 1H) 14.07 3 dipropyl carbonate 1H NMR (400MHz, (101MHz, DICHLOROMETHANE-d2) 6 = 4.04 (t, DICHLOROMETHANE-d2) 6 =
J=6.7 Hz, 2H), 1.66 (sxt, J=7.1 Hz, 2H), 155.98, 69.83, 22.66, 10.53 0.93 (t, J=7.4 Hz, 3H) 4 methyl propyl carbonate 3.90 (t, J=6.7 Hz, 2H), 3.57 (s, 3H), 1.50 155.42, 68.95, 53.88, 21.56, 9.54 (sxt, J=7.1 Hz, 2H), 0.77 (t, J=7.5 Hz, 3H) diisopropyl carbonate (400MHz, DICHLOROMETHANE-d2) 6 (101MHz, = 4.79 (spt, J=6.3 Hz, 1H), 1.23 (d, DICHLOROMETHANE-d2) 6 =
J=6.3 Hz, 6H) 154.79, 71.68, 22.18 6 isopropyl methyl 4.70 (spt, J=6.4 Hz, 1H), 3.59 (s, 3H), 154.92, 71.35, 53.84, 21.29 carbonate 1.13 (d, J=6.4 Hz, 6H) Table 1 Solvent Name 1H NMR 13C NMR
No (400MHz, CHLOROFORM-d) 6 = (101MHz, CHLOROFORM-d) 6=
7 ethyl dodecyl carbonate 4.16 (q, J=7.3 Hz, 2H), 4.09 (t, J=6.7 Hz, 155.17, 67.81, 63.56, 31.81, 2H), 1.63 (quin, J=7.1 Hz, 2H), 1.28 (t, 29.53, 29.52, 29.45, 29.40, 29.24, J=7.2 Hz, 3H), 1.39- 1.20 (m, 18H), 29.13, 28.59, 25.61, 22.57, 14.13, 0.85 (t, J=6.9 Hz, 3H) 13.95 8 ethyl propyl carbonate 4.03 (q, J=7.1 Hz, 2H), 3.94 (t, J=6.7 Hz, 154.93, 68.91, 63.26, 21.70, 2H), 1.55 (sxt, J=7.1 Hz, 2H), 1.15 (t, 13.84, 9.74 J=7.2 Hz, 3H), 0.82 (t, J=7.5 Hz, 3H) 9 ethyl isopropyl carbonate 4.68 (spt, J=6.4 Hz, 1H), 4.00 (q, J=7.1 154.26, 71.00, 63.18, 21.29, Hz, 2H), 1.13- 1.09 (m, 9H) 13.80 diisobutyl carbonate 3.80 (d, J=6.8 Hz, 2H), 1.87 (nonuplet, 155.29, 73.57, 27.58, 18.63 J=6.7, 1H), 0.85 (d, J=7.1 Hz, 6H) 11 isobutyl methyl 3.78 (d, J=6.6 Hz, 2H), 3.63 (s, 3H), 155.59, 73.65, 54.11, 27.47, carbonate 1.83 (nonuplet, J=6.8 Hz, 1H), 0.81 (d, 18.45 J=6.8 Hz, 6H) 12 dipentyl carbonate 4.03 (t, J=6.7 Hz, 2H), 1.59 (quin, J=6.9 155.20, 67.64, 28.19, 27.65, Hz, 2H), 1.34- 1.19 (m, 4H), 0.82 (br t, 22.08, 13.62 J=6.8 Hz, 3H) 13 methyl pentyl carbonate 4.04 (t, J=6.7 Hz, 2H), 3.68 (s, 3H), 1.58 155.67, 67.89, 54.24, 28.15, (quin, J=7.0 Hz, 2H), 1.35- 1.13 (m, 27.60, 22.05, 13.61 4H), 0.82 (t, J=7.0 Hz, 3H) 14 di(2-ethylhexyl) 4.11 - 3.93 (m, 2H), 1.68- 1.53(m, 1H), 155.68, 70.25, 38.81, 30.07, carbonate 1.48- 1.13 (m, 8H), 0.88 (t, J=7.5 Hz, 28.82, 23.44, 22.88, 13.92, 10.80 6H) 2-ethylhexyl methyl 4.04 - 3.89 (m, 2H), 3.67 (s, 3H), 1.59- 155.76, 70.10, 54.19, 38.68, carbonate 1.41 (m, 1H), 1.36- 1.06 (m, 8H), 0.81 29.94, 28.67, 23.29, 22.70, 13.69, (br t, J=7.5 Hz, 6H) 10.60 16 methyl 2-pentyl 4.67 (sxt, J=6.2 Hz, 1H), 3.66 (s, 3H), 155.27, 74.85, 54.06, 37.76, carbonate 1.61 - 1.46 (m, 1H), 1.45- 1.19 (m, 3H), 19.59, 18.28, 13.54 1.17 (d, J=6.1 Hz, 3H), 0.82 (t, J=7.2 Hz, 3H) 17 di(2-pentyl) carbonate 4.60 (sxt, J=6.2 Hz, 1H), 1.55- 1.41 (m, 154.29, 74.07, 37.77, 19.54 (d, 1H), 1.39- 1.14 (m, 3H), 1.10 (d, J=6.1 J=2.2 Hz), 18.27 (br d, J=2.2 Hz), Hz, 3H), 0.77 (t, J=7.2 Hz, 3H) 13.46 18 2-butyl methyl carbonate 4.52 (sxt, J=6.2 Hz, 1H), 3.59 (s, 3H), 155.14, 75.98, 53.84, 28.37, 1.71 - 1.29 (m, 2H), 1.09 (d, J=6.4 Hz, 18.87, 9.07.
3H), 0.76 (t, J=7.5 Hz, 3H) 19 di(2-butyl) carbonate 4.58 (sxt, J=6.3 Hz, 1H), 1.63- 1.39 (m, 154.45, 75.68 (br d, J=1.5 Hz), 2H), 1.16 (d, J=6.4 Hz, 3H), 0.83 (t, 28.59, 19.14 (br d, J=3.7 Hz), J=7.5 Hz, 3H) 9.35 (br d, J=2.9 Hz) 2-ethylbutyl methyl 4.01 (d, J=5.6 Hz, 2H), 3.72 (s, 3H), 155.88, 69.93, 54.38, 40.27, carbonate 1.49 (spt, J=6.1 Hz, 1H), 1.33 (quin, 22.90, 10.75 J=7.2 Hz, 4H), 0.85 (t, J=7.5 Hz, 6H) 21 di(2-ethylbutyl) 3.99 (d, J=6.1 Hz, 2H), 1.50 (spt, J=6.1 155.58, 69.73, 40.27, 22.88, carbonate Hz, 1H), 1.32 (nonuplet, J=7.3, 14.6 Hz, 10.71 4H), 0.84 (t, J=7.6 Hz, 6H) Table 1 Solvent Name 1H NMR 13C NMR
No (400MHz, CHLOROFORM-d) 6 = (101MHz, CHLOROFORM-d) 6=
22 isobutyl isopropyl 4.83 (spt, J=5.9 Hz, 1H), 3.86 (d, J=6.4 154.75, 73.54, 71.43, 27.67, carbonate Hz, 2H), 1.93 (nonuplet, J=6.5 Hz, 1H), 21.63, 18.79 1.25 (d, J=6.1 Hz, 6H), 0.91 (d, J=6.8 Hz, 6H) 23 2-cyanoethyl butyl 4.26 (t, J=6.2 Hz, 1H), 4.10 (t, J=6.7 Hz, 154.28, 116.42, 68.18, 61.51, carbonate 1H), 2.70 (t, J=6.2 Hz, 1H), 1.60 (quin, 30.24, 18.55, 17.74, 13.28 J=7.1 Hz, 1H), 1.34 (sxt, J=7.4 Hz, 1H), 0.88 (t, J=7.3 Hz, 2H) 24 2-methoxyethyl isobutyl 4.23 - 4.19 (m, 2H), 3.85 (d, J=6.6 Hz, 155.12, 73.86, 70.00, 66.43, carbonate 2H), 3.57 - 3.53 (m, 2H), 3.32 (s, 3H), 58.69, 27.54, 18.65 1.90 (nonuplet, J=6.6 Hz, 1H), 0.88 (d, J=6.6 Hz, 6H) 25 (2-trimethylsilyloxy)ethyl 4.12 (t, J=4.8 Hz, 2H), 4.07 (t, J=6.4 Hz, 155.15, 68.48, 67.59, 60.32, butyl carbonate 2H), 3.73 (t, J=4.9 Hz, 2H), 1.58 (quin, 30.50, 18.71, 13.41, -0.78 J=7.1 Hz, 2H), 1.34 (sxt, J=7.4 Hz, 2H), 29Si NMR (79MHz, 0.87 (t, J=7.3 Hz, 3H), 0.06 (s, 9H) CHLOROFORM-d) 6 = 19.31.
26 di(2-methoxyethyl) 4.18 - 4.05 (m, 2H), 3.52 -3.40 (m, 2H), 154.70, 69.69, 66.41, 58.37 carbonate 3.22 (s, 3H) 27 2-isopropoxyethyl methyl 4.15 - 4.02 (m, 2H), 3.61 (s, 3H), 3.50- 155.37, 71.51, 66.96, 65.28, carbonate 3.46 (m, 2H), 3.45 (spt, J=6.1 Hz, 1H), 54.16, 21.49 0.99 (d, J=6.1 Hz, 6H) 28 di(2-isopropoxyethyl) 4.32 - 4.01 (m, 2H), 3.56 - 3.50 (m, 2H), 154.93, 71.65, 67.01, 65.35, carbonate 3.49 (spt, J=6.1 Hz, 1H), 1.04 (d, J=6.2 21.65 Hz, 6H) 29 di(2-(2- 4.06 (t, J=4.5 Hz, 2H), 3.50 (t, J=4.5 Hz, 154.44, 71.23, 69.86, 68.24, methoxyethoxy)ethyl) 2H), 3.46 - 3.39 (m, 2H), 3.36 - 3.27 (m, 66.33, 58.30 carbonate 2H), 3.15 (s, 3H) Measurement of anodic dissolution of aluminum current collector
Example 5 (comparative): anodic dissolution of aluminum current collector in LiFSI-EC-DEC electrolyte
of fluoroethylene carbonate was added.
steps (1 hour of chronoamperaometry at 4.0, 4.1, 4.2...5.5 V). The results of this experiment can be seen in FIG.
1. Already at 4.3 V a significant appearance of current is observed, which indicates anodic dissolution. Accordingly, this electrolyte cannot be used for batteries where the potential of the cathode surpasses 4.3 V.
Example 6 (comparative): anodic dissolution of aluminum current collector in LiFTFSI-EC-DEC electrolyte
Already at 4.1 V a significant appearance of current is observed, which indicates anodic dissolution. Accordingly, this electrolyte cannot be used for batteries where the potential of the cathode surpasses 4.2 V.
Example 7 (comparative): anodic dissolution of aluminum current collector in LiTFSI-EC-DEC electrolyte
(available from 3MTm) in a conventional industrial solvent mixture of ethylene carbonate and diethyl carbonate, EC/DEC, in a volume ration of 3:7, and 2 wt% of fluoroethylene carbonate, as an electrolyte. The results of this experiment can be seen on FIG. 3. Already at 4.1 V, a significant appearance of current is observed, which indicates anodic dissolution. Accordingly, this electrolyte cannot be used for batteries where the potential of the cathode surpasses 4.2 V.
Example 8: Suppression of anodic dissolution of aluminum current collector in LiFSI-diisobutyl carbonate electrolyte
On all potentials tested (4-5.5V), the current density stays well below 1uA/cm2, meaning this electrolyte can be used inter alia with cathodes with a cut off potential of at least at 5.5 V.
Example 9: Suppression of anodic dissolution of aluminum current collector in LiFTFSI-diisobutyl carbonate electrolyte
On all potentials tested (4-5.5V), the current density stays well below 1uA/cm2, meaning this electrolyte can be used inter alia in battery systems where the voltage surpasses 5.5 V. As mentioned, electrolytes prepared from conventional solvents containing FSI
typically become unsafe when the operating voltage surpasses 4.3 V (see Examples 5 to 7).
Example 10: Suppression of anodic dissolution of aluminum current collector in LiTFSI-diisobutyl carbonate electrolyte
On all potentials tested (4-5.5V), the current density stays below 1uA/cm2, meaning this electrolyte can be used inter alia in battery systems where the voltage surpasses 5.5 V.
Examples 11-54: Starting potentials of anodic dissolution of various electrolytes
Table 2 Example Solvent No. Additives Conc. Starting potential (from table Salt of anodic 1) dissolution [V]
none EC/DEC (3:7 vol) 1M LiFSI 4.3 (comp) + 2 wt% FEC
6 none EC/DEC (3:7 vol) 1M LiFTFSI 4.2 (comp) + 2 wt% FEC
7 none EC/DEC (3:7v01) 1M LiTFSI 4.2 (comp) + 2 wt% FEC
8 10 2 wt% FEC 1M LiFSI >5.5 9 10 2 wt% FEC 1M LiFTFSI >5.5 10 2 wt% FEC 1M LiTFSI >5.5 11 1 2 wt% FEC 1M LiFSI >5.5 12 2 2 wt% FEC 1M LiFSI 5 13 3 2 wt% FEC 1M LiFSI 4.7 14 4 2 wt% FEC 1M LiFSI 4.5 5 2 wt% FEC 1M LiFSI 4.8 16 6 2 wt% FEC 1M LiFSI 4.6 17 7 2 wt% FEC 1M LiFSI >5.5 18 8 2 wt% FEC 1M LiFSI 4.5 19 9 2 wt% FEC 1M LiFSI 4.5 11 2 wt% FEC 1M LiFSI 4.6 21 12 2 wt% FEC 1M LiFSI 4.9 22 13 2 wt% FEC 1M LiFSI 4.5 23 14 2 wt% FEC 1M LiFSI >5.5 24 15 2 wt% FEC 1M LiFSI 5.0 16 2 wt% FEC 1M LiFSI 4.7 26 17 2 wt% FEC 1M LiFSI 5.5 27 18 2 wt% FEC 1M LiFSI 4.7 28 19 2 wt% FEC 1M LiFSI 5.3 29 20 2 wt% FEC 1M LiFSI 5 21 2 wt% FEC 1M LiFSI 5.1 31 22 2 wt% FEC 1M LiFSI 4.5 32 10 5 v/v% EC 1M LiFSI >5.5 + 2 wt% FEC
33 10 10 v/v% EC 1M LiFSI 5.2 + 2 wt% FEC
34 10 15 v/v % EC 1M LiFSI 4.4 + 2 wt% FEC
10 20 v/v% EC 1M LiFSI 4.2 + 2 wt% FEC
Table 2 Example Solvent No. Additives Conc. Starting potential (from table Salt of anodic 1) dissolution [V]
36 10 30 v/v% EC 1M LiFSI 4.1 + 2 wt% FEC
37 10 70 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.2 + 2 wt% FEC
38 10 50 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.3 + 2 wt% FEC
39 10 30 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.7 + 2 wt% FEC
40 10 20 v/v% EC/DEC (3:7 vol) 1M LiFSI
5.2 + 2 wt% FEC
41 14 75 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.2 + 2 wt% FEC
42 14 50 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.4 + 2 wt% FEC
43 14 25 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.4 + 2 wt% FEC
44 15 70 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.4 + 2 wt% FEC
45 15 50 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.4 + 2 wt% FEC
46 15 30 v/v% EC/DEC (3:7 vol) 1M LiFSI
4.4 + 2 wt% FEC
47 15 20 v/v% EC/DEC (3:7 vol) 1M LiFSI >5.5 + 2 wt% FEC
48 23 2 wt% FEC 1M LiFSI 5.1 49 24 2 wt% FEC 1M LiFSI 5.1 50 25 2 wt% FEC 1M LiFSI 5.4 51 26 2 wt% FEC 1M LiFSI 4.8 52 27 2 wt% FEC 1M LiFSI 4.9 53 28 2 wt% FEC 1M LiFSI 5.2 54 29 2 wt% FEC 1M LiFSI 4.9 Button cell charge-discharge tests Example 55 (comparative): Unsuccessful charging and discharging of LCO in LiFSI-EC-DEC electrolyte
(vapour grown carbon nanotubes), carbon black and polyvinylidene fluoride (PVDF) in a ratio 89:3:3:5 by weight in N-methyl-2-pyrrolidone (NMP). The mixture was then coated on a 15 pm thick non-coated aluminum current collector, provided by UACJ. The electrode material was calendered, cut into discs and dried at 120 C in a vacuum oven for 12 h before use.
Example 56: Successful charging and discharging of LCO in LiFSI-diisobutyl carbonate electrolyte
Example 57: Successful charging and discharging of LCO in LiFSI-EC-diisobutyl carbonate electrolyte
Example 58 (comparative): Unsuccessful charging and discharging of LMN in LiFSI-EC-DEC electrolyte
The mixture was then coated on a 15 pm thickness of non-coated aluminum current collector, provided by UACJ.
The electrode material was calendered, cut into discs and dried at 120 C in a vacuum oven for 12 h before use.
Example 59: Successful charging and discharging of LMN in LiFSI-diisobutyl carbonate electrolyte
Example 60: Extended temperature range of a diisobutyl carbonate-based electrolyte compared to conventional solvent
This indicates that the electrolyte of the invention can be used at lower temperatures than conventional electrolytes without crystallisation.
Example 61: Full Li-ion cell
diisobutyl carbonate:10 % EC, 2% of FEC) and a conventional electrolyte of 1 M
LiPF6 in EC/DEC (3:7 vol) with 2% of FEC were tested.
coated on 15 pm thick aluminum current collector (as in example 55), provided by UACJ, as a cathode; Celgard Q20S1HX as separator membrane;
one of the above-listed electrolytes; and the above-prepared 16 mm disc of graphite electrode as an anode.
at C/24 rate. After that, the cells were subjected to long term cycling with charging at C/4, followed by a 30 min float at 4.4 V and C/4 discharge. The results of this experiment ¨ the discharge capacity of the cells versus cycle number - can be seen in FIG. 12. The LiPF6 electrolyte provides the highest starting discharge capacity, but then one can observe relatively linear diminution of the capacity over cycle number. LiFSI
in pure diisobutyl carbonate has approximately 10% less of the starting capacity, but degradation of the capacity is slower than in the case of LiPF6.
The addition of 10 % of EC to pure diisobutyl carbonate electrolyte increases the starting capacity, but the speed of degradation approaches to that of LiPF6.
in the solvents of the present invention in high voltage Li-ion batteries has been demonstrated, while the utilisation of LiFSI in conventional solvents is not possible for this battery system.
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Claims (63)
(a) a cathode comprising an aluminum current collector and having an upper potential limit of about 4.2 V or more vs a Li-metal reference electrode, (b) an anode, (c) a separator membrane separating the anode and the cathode, and (d) a low-corrosiveness non-aqueous electrolyte in contact with the anode and the cathode, wherein the battery has an upper voltage limit of about 4.2 V or more, wherein anodic dissolution of aluminum in the aluminum current collector is suppressed during battery operation at voltages up to said upper voltage limit, and wherein the electrolyte comprises, as a solvent, a carbonate compound of formula (I):
0 0 (l), wherein:
R1 represents a 03-024 alkyl, a 03-024 alkoxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), or a 04-024 w-O-alkyl oligo(propylene glycol), and R2 represents a 01-024 alkyl, a 01-024 haloalkyl, a 02-024 alkoxyalkyl, a 02-024 alkyloyloxyalkyl, a 03-024 alkoxycarbonylalkyl, a 01-024 cyanoalkyl, a 01-024 thiocyanatoalkyl, a 03-024 trialkylsilyl, a 04-024 trialkylsilylalkyl, a 04-024 trialkylsilyloxyalkyl, a 03-024 w-O-alkyl oligo(ethylene glycol), a 04-024 w-O-alkyl oligo(propylene glycol), a 05-024 w-O-trialkylsilyl oligo(ethylene glycol), or a 06-024 w-O-trialkylsilyl oligo(propylene glycol), and a conducting salt dissolved in said solvent.
or more, preferably 6 or more, more preferably 7 or more, yet more preferably 8 or more, and most preferably 9 or more, and/or 24 or less, preferably 20 or less, more preferably 16 or less, yet more preferably 14 or less, even more preferably 12 or less, and most preferably 10 or less.
= LiCl04;
= LiP(CN)0F6_0õ where a is an integer from 0 to 6, preferably LiPF6;
= LiB(CN)pF443, where 6 is an integer from 0 to 4, preferably LiBF4;
= LiP(CnF2n+i)yF6_y, where n is an integer from 1 to 20, and y is an integer from 1 to 6;
= LiB(CnF2n+i )5F4_5, where n is an integer from 1 to 20, and 6 is an integer from 1 to 4;
= Li2Si(CnF2n-o )EF6-E, where n is an integer from 1 to 20, and is an integer from 0 to 6;
= lithium bisoxalato borate;
= lithium difluorooxalatoborate; or = a compound represented by one of the following general formulas:
\ ......00 4 0 0 5 0 0 __ ( 11 0 0 S R,.... /'/ \\
..õR
4 11 CY \ 1 05 S S
R--S--0 N--S--R4 im--0--n // \\
1 1 \ 3 / 11 / 11 0 I 3 0 R
0 0 N'l--'0------S-----R R R4 R7 \R6 R6 \R5 R6 \R5 R_ ,N 4 \ICI5t3 N(G..3 R5 N 4 N
N-c 'IR N-c 'IR (CR3 N'C----------R4 , or N--N =
wherein:
R3 represents: Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, Al, hydrogen, or an organic cation; and R4, R5, R6, R7, R8 represent: cyano, fluorine, chlorine, branched or linear alkyl radical with 1-24 carbon atoms, perfluorinated linear alkyl radical with 1-24 carbon atoms, aryl, heteroaryl, perfluorinated aryl, or heteroaryl;
or a derivative thereof.
= an agent that improves solid electrolyte interphase and cycling properties;
= an unsaturated carbonate that improves stability at high and low voltages, and/or = an organic solvent that diminishes viscosity and increases conductivity.
w/w, and/or at most about 20%
w/w, at most about 15% w/w, at most about 10% w/w, or at most about 7% w/w of the total weight of the electrolyte.
v/v, at least about 5% v/v, or at least about 7% v/v, and/or at most about 80% v/v, at most about 50% v/v, at most about 20% v/v, at most about 15% v/v, at most about 10% v/v, or at most about 7% v/v of the total volume of the electrolyte.
= about 5% v/v of EC, = about 10% v/v of EC, = about 15% v/v of EC, = about 20% v/v of EC, = about 30% v/v of EC, = about 20% v/v of a mixture of EC and DEC, = about 25% v/v of a mixture of EC and DEC, = about 30% v/v of a mixture of EC and DEC, = about 50% v/v of a mixture of EC and DEC, = about 70% v/v of a mixture of EC and DEC, or = about 75% v/v of a mixture of EC and DEC, wherein said mixture preferably has an EC:DEC volume ratio of from about 1:10 to about 1:1, preferably of about 3:7, all w/w% being based on the total weight of the electrolyte and all v/v% being based on the total volume of the electrolyte.
v/v, and most preferably at least about 95%, of the total volume of the electrolyte.
= a lithiated oxide of transition metal (s) such as LNO (LiNi02), LMO
(LiMn204), LiCoxl\lii_x02wherein x is from 0.1 to 0.9, LMC (LiMnCo02), LiCOVIn2_,(04, NMC (LiNiNnyCoz02), or NCA
(LiNixCoAlz02), or = a lithium compound of transition metal(s) and a complex anion, such as LFP (LiFePO4), LNP
(LiNiPO4), LMP (LiMnPO4), LCP (LiCoPO4), Li2FCoPO4; LiCociFexNliyMnzPO4, or Li2MnSia4.
0 0 (l), wherein Ri represents a C3-C24 alkyl, a C3-C24 alkoxyalkyl, a C3-C24 w-O-alkyl oligo(ethylene glycol), or a C4-C24 w-O-alkyl oligo(propylene glycol), and R2 represents a Cl-C24 alkyl, a Cl-C24 haloalkyl, a C2-C24 alkoxyalkyl, a C2-C24 alkyloyloxyalkyl, a C3-C24 alkoxycarbonylalkyl, a Ci-C24 cyanoalkyl, a Ci-C24 thiocyanatoalkyl, a C3-C24 trialkylsilyl, a C4-C24 trialkylsilylalkyl, a C4-C24 trialkylsilyloxyalkyl, a C3-C24 w-O-alkyl oligo(ethylene glycol), a C4-C24 w-O-alkyl oligo(propylene glycol), a C5-C24 w-O-silyl oligo(ethylene glycol), or a C6-C24 w-O-silyl oligo(propylene glycol), with proviso that when R2 is a Ci-C9 alkyl, Ri represents a Ci0-C24 alkyl, a C3-C24 alkoxyalkyl, a C3-C24 w-0-alkyl oligo(ethylene glycol), or a C4-C24 w-O-alkyl oligo(propylene glycol).
5 or more, preferably 6 or more, more preferably 7 or more, yet more preferably 8 or more, and most preferably 9 or more, and/or 24 or less, preferably 20 or less, more preferably 16 or less, yet more preferably 14 or less, even more preferably 12 or less, and most preferably 10 or less.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1904075A FR3095204A1 (en) | 2019-04-16 | 2019-04-16 | CARBONATE SOLVENTS FOR NON-AQUEOUS ELECTROLYTES, NON-AQUEOUS ELECTROLYTES AND ELECTROCHEMICAL DEVICES, AND METHODS FOR MANUFACTURING THEM |
| FR1904075 | 2019-04-16 | ||
| PCT/IB2020/053563 WO2020212872A1 (en) | 2019-04-16 | 2020-04-15 | Carbonate solvents for non-aqueous electrolytes for metal and metal-ion batteries |
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| Publication Number | Publication Date |
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| CA3134636A1 true CA3134636A1 (en) | 2020-10-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA3134636A Pending CA3134636A1 (en) | 2019-04-16 | 2020-04-15 | Carbonate solvents for non-aqueous electrolytes for metal and metal-ion batteries |
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| Country | Link |
|---|---|
| US (1) | US20220209301A1 (en) |
| EP (1) | EP3956288A1 (en) |
| JP (1) | JP7624402B2 (en) |
| KR (1) | KR20210150435A (en) |
| CN (1) | CN113795963A (en) |
| CA (1) | CA3134636A1 (en) |
| FR (1) | FR3095204A1 (en) |
| WO (1) | WO2020212872A1 (en) |
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| US20240297343A1 (en) * | 2021-06-23 | 2024-09-05 | Central Glass Co., Ltd. | Nonaqueous electrolyte solution, nonaqueous sodium ion battery, nonaqueous potassium ion battery, method for producing nonaqueous sodium ion battery, and method for producing nonaqueous potassium ion battery |
| KR102752003B1 (en) * | 2022-03-31 | 2025-01-09 | 한국생산기술연구원 | Heterogeneous base catalyst for use in preparing carbonate derivative, and method of preparing carbonate derivative using same |
| EP4322261A4 (en) * | 2022-06-17 | 2025-06-11 | Contemporary Amperex Technology (Hong Kong) Limited | Additive and preparation method therefor and use thereof, and positive electrode plate and preparation method therefor |
| CN115117452B (en) * | 2022-08-30 | 2022-12-06 | 深圳新宙邦科技股份有限公司 | Lithium ion battery |
| KR102822482B1 (en) * | 2022-09-07 | 2025-06-20 | 한국과학기술연구원 | Organic carbonate-based high flash point electrolyte |
| WO2024195306A1 (en) * | 2023-03-22 | 2024-09-26 | 株式会社村田製作所 | Secondary battery |
| JP7839125B2 (en) * | 2023-04-06 | 2026-04-01 | 信越化学工業株式会社 | Non-aqueous electrolyte and non-aqueous electrolyte secondary battery |
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| FR2683524A1 (en) | 1991-11-08 | 1993-05-14 | Centre Nat Rech Scient | DERIVATIVES OF BIS (PERFLUOROSULFONYL) METHANES, THEIR METHOD OF PREPARATION, AND THEIR USES. |
| CA2197056A1 (en) | 1997-02-07 | 1998-08-07 | Hydro-Quebec | New ionically conductive material with improved conductivity and stability |
| JP2000228216A (en) * | 1999-02-08 | 2000-08-15 | Denso Corp | Non-aqueous electrolyte and non-aqueous electrolyte secondary battery |
| US6866966B2 (en) * | 1999-08-03 | 2005-03-15 | Ube Industries, Ltd. | Non-aqueous secondary battery having enhanced discharge capacity retention |
| JP2003036884A (en) * | 2001-07-19 | 2003-02-07 | Sony Corp | Non-aqueous electrolyte and non-aqueous electrolyte battery |
| JP4042034B2 (en) * | 2002-02-01 | 2008-02-06 | 株式会社ジーエス・ユアサコーポレーション | Non-aqueous electrolyte battery |
| JP4397810B2 (en) * | 2002-08-07 | 2010-01-13 | 旭化成ケミカルズ株式会社 | Method for producing carbonate ester |
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| US11345657B2 (en) | 2016-10-19 | 2022-05-31 | Hydro-Quebec | Sulfamic acid derivatives and processes for their preparation |
-
2019
- 2019-04-16 FR FR1904075A patent/FR3095204A1/en not_active Withdrawn
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2020
- 2020-04-15 EP EP20720529.5A patent/EP3956288A1/en not_active Withdrawn
- 2020-04-15 CN CN202080028545.7A patent/CN113795963A/en active Pending
- 2020-04-15 US US17/602,590 patent/US20220209301A1/en active Pending
- 2020-04-15 JP JP2021558568A patent/JP7624402B2/en active Active
- 2020-04-15 CA CA3134636A patent/CA3134636A1/en active Pending
- 2020-04-15 WO PCT/IB2020/053563 patent/WO2020212872A1/en not_active Ceased
- 2020-04-15 KR KR1020217034874A patent/KR20210150435A/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
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| WO2020212872A1 (en) | 2020-10-22 |
| KR20210150435A (en) | 2021-12-10 |
| US20220209301A1 (en) | 2022-06-30 |
| FR3095204A1 (en) | 2020-10-23 |
| JP2022529217A (en) | 2022-06-20 |
| CN113795963A (en) | 2021-12-14 |
| EP3956288A1 (en) | 2022-02-23 |
| JP7624402B2 (en) | 2025-01-30 |
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