Patent Application
20240178451
The invention relates to an electrolyte composition for sodium-ion battery, and uses thereof as a non-aqueous liquid electrolyte in a sodium-ion battery.
The sodium-ion (Na-ion) technology is a promising alternative candidate for next-generation batteries, especially in the stationary energy storage field due to the high natural abundance and low cost of sodium as compared to lithium. This has led over the last decade to blooming research on various components of sodium-ion batteries developing new and superior electrode materials for optimized Na-ion battery systems. Two types of technology based either on polyanionic, e.g., Na3V2(PO4)2F3 or layered e.g., O3 NaNi0.5Mn0.5O2 and P2 Na0.67Mn0.5Fe0.5O2 compounds have emerged, with the former being the most performing in terms of power rate, cycle life and specific energy.
However, for practical applications, other features, such as operation at different temperatures/climatic conditions, safety, self-discharge and durability that strongly depend on the nature and stability of interphases namely solid electrolyte interphase (SEI) and cathode electrolyte interphase (CEI) must be satisfied. This called for intensive research on the nature of the electrolyte used. At the early stage, researchers naively believe that simple extrapolation of what has been used for the Li-ion technology could be used just by changing the Li-salt to sodium salt. But this was without counting that the solubility of Na-based organic/inorganic products that compose the Na-derived SEI/CEI, is different compared with those of Li-counterparts owing to the milder acidity of Na+ as compared to Li+.
In light of such remarks, the inventors experienced that Na3V2(PO4)2F3/hard carbon (C) cells based on classical mixtures of ethylene carbonate (EC), propylene carbonate (PC) and dimethyl carbonate (DMC) with a 1 mol/L NaPF6 electrolytes were performing exceedingly well at room temperature, but were showing bad performances at 55° C. in terms of cycling and self-discharge.
One solution developed by the inventors was to implement a specific electrolyte based on a mixture of EC-PC and NaPF6 to which was added a few additives: sodium difluoro(oxalate)borate (NaODFB), succinonitrile N≡C—(CH2)2—C≡N (SN), 1,3-propane sultone (PS), and vinylene carbonate (VC).
However, this electrolyte has some drawbacks, such as its inability to be used with commercial polyolefin separators because of a poor wettability, high viscosity and the decrease of the cell power capability (high resistance SEI).
With the aim to wet the commercial polyolefin separators, the inventors implemented another specific electrolyte based on ethylene carbonate (EC) and dimethyl carbonate (DMC) with a 1 mol/L NaPF6 to which the following additives were added: NaODFB, VC and Tris(trimethylsilyl)phosphite (TMSPi).
However, when used in commercial cells, it was observed a continuous raise in cell pressure upon cycling leading to the circuit interrupt device (CID) of the cell to break and to cell failure.
The aim of the invention is to obviate these drawbacks.
The purpose of the invention is to provide an electrolyte composition for Na-ion battery which exhibits better performance in terms of power rate, cycle life and specific energy, while keeping good wettability properties and triggering a reduced pressure formation.
Thus, the invention relates to an electrolyte composition comprising at least one sodium salt dissolved in a solvent and a combination of additives, wherein:
The inventors unexpectedly found that combining succinonitrile helps in protecting the positive electrode by forming stable CEI and reduce the oxidation of electrolyte solvent, thereby reduce the formation of gaseous bi-products to overcome the raising pressure issue upon cycling. Furthermore, the electrolyte composition of the invention shows better performance in terms of power rate, cycle life and/or specific energy, while keeping good wettability properties.
According to an embodiment of the invention, the amount of TMSPi ranges from 0.05 to 10 wt %, based on the total weight of the sodium salt and the solvent. Notably, the amount of TMSPi may range from 0.05 to 5 wt %, preferably from 0.1 to 1 wt %, and even more preferably the amount of TMSPi is around 0.2 wt %, again based on the total weight of the sodium salt and the solvent.
It is believed, without wishing to be limited by such finding, that the succinonitrile contributes to the passivation of the positive electrode either by the formation of a monolayer of chemisorbed nitrile molecules on the transition metal oxide surface or by an oxidative decomposition.
According to an embodiment of the invention, the amount of succinonitrile ranges from 0.1 to 5 wt %, based on the total weight of the sodium salt and the solvent. Notably, the amount of succinonitrile may range from 1 to 5 wt %, preferably from 2 to 4 wt %, and more preferably the amount of succinonitrile may be around 3 wt %, again based on the total weight of the sodium salt and the solvent.
According to an embodiment of the invention, the combination of additives further comprises at least one additional additive chosen in a group which comprises or consists of vinylene carbonate, vinylethylene carbonate and difluoro(oxalato)borate (NaODFB) and mixture thereof.
NaODFB is a film-forming additive that undergoes reductive decomposition on the negative electrode leading to its passivation. It is believed that the decomposition products of NaODFB efficiently contribute to the SEI composition and provide protection against parasitic reactions on the negative electrode.
The amount of NaODFB may range from 0.05 to 10 wt %, based on the total weight of the sodium salt and the solvent. Preferably, the amount of NaODFB ranges from 0.05 to 5 wt %, and in particular may range from 0.05 to 1 wt %, based on the total weight of the sodium salt and the solvent. An amount of NaODFB around 0.5 wt %, based on the total weight of the sodium salt and the solvent, is particularly preferred.
The addition of vinylene carbonate to the electrolyte composition of the invention may further enhance the electrolyte performance due to the synergetic effect between vinylene carbonate and TMSPi. Besides, vinylene carbonate can help to minimize the degradation of DMC via the formation of an elastomer, and limiting the amount of soluble species moving to the positive electrode.
Especially, the amount of vinylene carbonate and/or the amount of vinylethylene carbonate each ranges from 0.1 to 10 wt %, based on the total weight of the sodium salt and the solvent. Notably, the amount of vinylene carbonate and/or the amount of vinylethylene carbonate ranges from 1 to 5 wt %, based on the total weight of the sodium salt and the solvent. In particular, the amount of vinylene carbonate and/or the amount of vinylethylene carbonate each ranges from 2 to 5 wt %, based on the total weight of the sodium salt and the solvent.
Even more, the amount of vinylene carbonate and/or the amount of vinylethylene carbonate each is 3 wt %, based on the total weight of the sodium salt and the solvent.
According to a particular embodiment of the invention, the combination of additives comprises TMSPi, SN, NaODFB and vinylene carbonate.
According to an embodiment of the invention, the solvent is a mixture of at least a first and a second compounds, said first compound being ethylene carbonate and said second compound being selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, propylene carbonate, a carboxylate ester such as ethyl propionate and methyl acetate, diglyme and 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether.
Especially, the second compound is selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate and propylene carbonate. In particular, the second compound is dimethyl carbonate or propylene carbonate.
The volume ratio of the first compound to the second compound may range from 1:20 to 20:1, especially from 1:9 to 5:1. In particular, the volume ratio is around 1:1.
In a particular embodiment, the mixture of at least two compounds is a mixture of ethylene carbonate and propylene carbonate, preferably in a volume ratio of 1:1.
Preferably, the solvent further comprises a third compound selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, propylene carbonate, a carboxylate ester such as ethyl propionate and methyl acetate, diglyme and 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether.
In particular, said third compound is selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, a carboxylate ester such as ethyl propionate and methyl acetate, diglyme and diethyl carbonate.
The volume ratio of the first compound and second compound to the third solvent may range from 1:1:1 to 1:1:20. In particular the first, second and third compounds are mixed according to a volume ratio of 1:1:1, 1:1:8 or 1:1:2.
Preferably, the solvent further comprises a fourth compound selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, propylene carbonate, a carboxylate ester such as ethyl propionate and methyl acetate, diglyme and 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether.
In particular, said fourth compound is selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, a carboxylate ester such as ethyl propionate and methyl acetate, diglyme and diethyl carbonate.
A preferred solvent mix comprises ethylene carbonate, propylene carbonate, dimethyl carbonate and methyl acetate.
The respective volume ratio of the first, second and third compounds to the fourth compound may range from 1:1:1.84:0.16 to 1:1:30:20.
In another embodiment of the invention, the solvent is mixture of linear and cyclic carbonates. Preferably, the solvent is a mixture of at least a first and a second compositions, said first composition being ethylene carbonate and/or propylene carbonate, and said second composition being selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, a carboxylate ester such as methyl acetate and ethyl propionate, diglyme, 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether and mixture thereof.
In particular, the second composition is selected in the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, a carboxylate ester such as methyl acetate and ethyl propionate and diglyme.
In a preferred embodiment, the first composition is a mixture of ethylene carbonate and propylene carbonate. In that case, the volume ratio of ethylene carbonate to propylene carbonate is preferably 1:1.
The volume ratio of the first composition to the second composition may range from 1:20 to 5:1, with preference from 1:20 to 1:1. Preferably, the volume of the second composition (linear carbonate(s)) is higher than the one of the first composition (cyclic carbonate(s)) in order to reduce the viscosity of the electrolyte composition.
In another embodiment the solvent comprises a carboxylate ester, which may have less than 20 carbon atoms, preferably less than 10 carbon atoms such as methyl acetate or ethyl propionate. Irrespective of the presence of 4 additives, an electrolyte composition with methyl acetate as a cosolvent provides advantage with respect to bulk conductivity, has less resistive interphases and exhibits less impedance. This is beneficial, inter alia, for low temperature (sub-zero) cycling as well as high power performance (for example about 84% in 10 min charge) or good rate capability. It has also been found that it particularly advantageous to use methyl acetate to replace some dimethyl carbonate.
The sodium salt may be chosen among the salts commonly used in non-aqueous electrolyte suited for Na-ion batteries. As examples of sodium salt, one can mention sodium hexafluorophosphate (NaPF6), sodium perchlorate (NaClO4), sodium bis (fluor sulfonyl) imide (NaFSI), sodium bis(trifluoromethanesulfonyl)imide (NaTFSI), sodium fluorosulfonyl-(trifluoromethanesulfonyl)imide (NAFTFSI), sodium bis(pentafluoroethanesulfonyl)imide (NaBETI), sodium tetrafluoroborate (NaBF4), and one of their mixture.
In particular, the sodium salt is NaPF6, preferably mixed with another sodium salt such as one of the above and in particular NaFSI, NaTFSI and NaFTFSI. The proportion of NaPF6 in respect of the other salt (s) is preferably in the range of 50 to 99 wt. %.
Preferably, the other sodium salt is present in a amount from 0.5 to 15 wt. %, preferably from 1 to 10 wt. %, in particular from 2 to 4 wt. % (e.g. around 3 wt. %) based on the total weight of the electrolyte solvent and salt.
The concentration of sodium salt in the electrolyte composition may range from about 0.1 to 3.0 mol/L and preferably from about 0.5 to 2.0 mol/L.
As a particular embodiment of the invention, the electrolyte composition comprises:
As a particular embodiment of the invention, the electrolyte composition comprises:
As a particular embodiment of the invention, the electrolyte composition comprises:
As a particular embodiment of the invention, the electrolyte composition comprises:
As a particular embodiment of the invention, the electrolyte composition comprises:
The invention also relates to the use of the electrolyte composition as defined above, as a non-aqueous liquid electrolyte in a Na-ion battery. In a preferred embodiment, the first cycle of charge is carried out at a temperature from 25° C. to 70° C., in particular 55° C. Especially, the temperature used for the first charge is equal or higher, preferably higher, than the one used for the subsequent charges, in order to obtain a more stable SEI.
Finally, the invention relates to a Na-ion battery comprising:
at least one negative electrode comprising a negative electrode active material and a current collector; and
at least one separator impregnated with a non-aqueous liquid electrolyte, said separator being placed between said positive electrode and said negative electrode;
wherein said non-aqueous liquid electrolyte is an electrolyte composition as defined above.
The positive electrode active material is a material capable of inserting sodium ions reversibly which may be chosen among oxides such as NaxMO2 in which M represents at least one metallic element selected from the group comprising Ni, Co, Mn, Fe, Cr, Ti, Cu, Zn, V, Al and Mg; and among phosphates such as NaTi2(PO4)3, Na3V2(PO4)3, Na3V2(PO4)2F3, Na2MnP2O7, Na2MnPO4F, Na1.5VPO4.8F0.7 and/or NaV1-xCrxPO4F. Among these positive electrode active materials, Na3V2(PO4)2F3, also named NVPF, Na2/3Mg1/3Mn2/3O2, and a mixture thereof, are particularly preferred.
In addition to the positive electrode active material, the positive electrode may further include a polymer binder and optionally an electronic conducting agent.
As an example of suitable polymer binders, a mention may be made of polyvinylidene difluoride (PVdF), poly(tetrafluoroethylene) (PTFE), cellulose fibers, cellulose derivatives such as starch, carboxymethyl cellulose (CMC), diacetyl cellulose, hydroxyethyl cellulose or hydroxypropyl cellulose, styrene butadiene rubber (SBR) and a mixture thereof. Among these binders, PVdF is preferred.
The conductive agent may be carbon black, Super P carbon black, acetylene black, ketjen black, channel black, natural or synthetic graphite, carbon fibers, carbon nanotubes, vapor grown carbon fibers or a mixture thereof.
The proportions, relatively to the total weight of the positive electrode, are preferably:
The negative electrode active material used for the negative electrode can be selected among carbon materials, in particular hard carbon, soft carbon, carbon nanofibers or carbon felt, antimony, tin, and phosphorus.
According to a preferred embodiment of the present invention, the negative electrode active material is a carbon material and said negative electrode further comprises a polymer binder which may be chosen among the same polymer binders as those mentioned above for the positive electrode, and preferably from PVdF or cellulose derivatives binders.
As mentioned for the positive electrode, the negative electrode may further include a conductive agent which may be chosen among the same conductive agent as those mentioned above for the positive electrode.
The positive and/or negative electrode may also include a current collector.
The current collectors of the positive and/or negative electrodes may comprise an electron conductive material, more particularly a metallic material which may be selected from the group consisting of aluminium, copper, nickel, titanium, steel and their alloys.
The separator may be a conventional polymer-based separator including polypropylene and/or polyethylene such as a Celgard® separator or glass fibers, such as a Whatman® borosilicate glass fiber separator, or a cellulose-based separator, such as a Dreamweaver® nonwoven nanofiber separator.
A Na-ion battery according to the invention may comprise a single electrochemical cell comprising two electrodes (i.e., one positive electrode and one negative electrode) separated by an electrolyte; or of a plurality of chemical cells assembled in series; or of a plurality of chemical cells assembled in parallel; or of a combination of the two assembly types.
Four electrolyte composition (EC1 to EC4) were prepared by mixing
The additives of compositions EC1 to EC4 are given in the following table (in wt % relatively to the total weight of the solvent and the salt):
EC1 to EC9 were prepared according to the same method described hereafter wherein the mass of the additives was adapted for each electrolyte solution.
In detail for EC3, 1 mL of EC (Dodochem®), 1 mL of PC (Dodochem®) and 1 mL DMC (Dodochem®) were added to a vial and mixed. The mass of the solvent was 3.59 g (1.32 g EC+1.2 g PC+1.07 g DMC). Subsequently, it was added 0.504 g of NaPF6 (Stella®) to reach the 1M of concentration. The total mass of this mixture was then 4.1 g. Accordingly, it was further added 123 mg of succinonitrile (Aldrich®), 123 mg of vinylene carbonate (Aldrich®), 21 mg of NaDFOB (Aldrich®) and 8 mg of TMSPi (Aldrich®). Succinonitrile is a waxy solid at room temperature (melting point at around)60° ° C., and was first heated to 70° C. allowing the appropriate mass to be extracted using a Pasteur pipet.
Other electrolyte solutions were also prepared (EC10 to EC14). These electrolyte solutions comprise the same additives and salt that EC3 but have a different solvent composition, as given by the below table. EC10 to EC14 were prepared with the same method described above for EC3 but with the adequate solvent (ethyl methyl carbonate, diethyl carbonate and diglyme from Sigma Aldrich®).
Electrochemical performances of electrolyte compositions EC1, and EC3, EC5 to EC14 were tested in coin cells having the following configuration.
The positive electrode was prepared by mixing Na3V2(PO4)2F3 (NVPF, mass loading: 12.6 mg/cm2), with polyvinylidinefluoride (PVdF, 3.0 wt. %) and carbon black (3.0 wt. %). The resulting mixture was dispersed in N-methylpyrrolidine (NMP) to form a homogeneous slurry, which then was casted onto a current collector made of an aluminium foil. The positive electrode was dried at 120° C. and then pressed by a roller machine.
The negative electrode was prepared by mixing hard carbon (mass loading 6.1 mg/cm2) with PVdF (3.0 wt. %) and carbon black (3.0 wt. %). The resulting mixture was dispersed in N-methylpyrrolidine (NMP) to form a homogeneous slurry, which then was casted onto a current collector made of an aluminium foil. The positive electrode was dried at 120° C. and then pressed by a roller machine.
The positive electrode and the negative electrode were cut into circular disc of 13 mm diameter and dried at 80° C. under vacuum (less than 100 mbar) for 24 hours. A separator (glass fiber separator Whatman®, GF/D) is soaked with 15-16 drops of one electrolyte composition from EC1, and EC3, EC5 to EC14. Then, the 2032 type coin cells were assembled in Argon atmosphere by stacking on a positive can the positive electrode, the separator, the negative electrode, a metal disc to provide pressure, a metal spring to provide homogenous pressure and sealed with a negative can, where water and oxygen content is less than 1 ppm. The 2032 type coin cells containing the electrolyte compositions EC1, and EC3, EC5 to EC14 correspond to Na-ion batteries Na-B1 to Na-B12, respectively, and correspondences are given in the table below:
The whole process was carried out at fixed temperature (55/25/0° C.), with a voltage range of 2.0 to 4.3 V.
The test procedure included the following steps:
The capacity (Q) of the 2032 type coin cell is calculated at the end (discharge) of the n−1th cycle, the nth cycle and the n+1th cycle. The ratio ((Qn−1-Qn)*100)/Qn−1 gives the capacity loss on self-discharge (in percentage) of the coin cell. The recovered capacity (in percentage) of the coin cell is calculated as the ratio (Qn+1*100)/Qn−1.
The charges/discharges curves of Na-ion battery Na-B2 at temperature 0° C., 25° C. and 55° C. are represented in
As shown, at temperatures 0° C. and 25° C., the charges/discharges curves for cycles 1 to 10 and cycles 12 to 21 overlap on each other. Accordingly, the recovered capacity is near 100%. Hence, at these temperatures there is no slippage in capacity showing the absence of parasitic reaction in positive and negative electrode, and therefore indicates the formation of stable solid electrolyte interphase (SEI) and cathode electrolyte interphase (CEI).
At temperature 55° C., the one-week resting period at full SoC causes only a slight capacity loss of 3%. This confirms the remarkable stability of SEI even at extreme conditions such as high temperature, which contribute to minimizing side reactions and thus preventing the consumption of the active materials (electrolyte, electrode materials etc.).
The value of discharge capacity of Na-ion battery NA-B2 is shown at
Importance to carry out the first cycle at high temperature (from room temperature to 70° C.) is shown through
Bring together, these results show that Na-ion battery Na-B2 enables to achieve very good cycling performances at the nominal temperature for the battery to be used (0° C. and 25° C.) as well as at high temperature (55° C.).
The inventors then compared the electrochemical performance between Na-ion batteries Na-B1 (comparative) and Na-B2 (invention) at 55° C. (
The inventors also compared the electrochemical performance between 2032 coin type cell and 18650 cell (see Example 3 for composition) both containing electrolyte composition EC3. The test procedure was applied in both cases (with 1C=˜1200 mAh.g−1 for the 18650 cell). The charge/discharge curves at 55° C. are represented on
The inventors tested different amounts of NaODFB in 2032 type coin cells and their impact on electrochemical performances. The electrochemical performances of Na-ion batteries Na-B2 to Na-B6 are represented on
From these results, one can conclude that all the Na-ion batteries Na-B2 to NB6 show very good electrochemical performances, and that the increasing the amount of NaODFB above 0.3 wt % has little impact on capacity loss and recovered capacity. Further, the inventors found that 0.5 wt % of NaODFB is the optimal quantity needed for the electrolyte formulation. Indeed, usage of lesser NaODFB results in less efficient formation of SEI (e.g., Na-B3 with 0.1% NaODFB) and usage of higher amount of NaODFB results in increase in cell impedance due to the growth of thicker SEI.
The inventors tested different amounts of succinonitrile in 2032 type coin cells and their impact on electrochemical performances. The electrochemical performances of Na-ion batteries Na-B2 and Na-B8 are represented on
Form this result, usage of 3 wt % of succinonitrile gives the better electrochemical performances.
The inventors tested different solvent compositions with different linear carbonate or a different ratio with DMC (Na-B10) for the electrolyte composition of Na-ion batteries. The electrochemical performances of Na-ion batteries Na-B8 to Na-B12 are represented on
Na-ion batteries Na-B8 to Na-B12 achieved very good cycling performances.
The usage of huge amount of electrode active material and electrolyte is a major reason for the production of large amount of gaseous bi-product in 18650 cells compared to 2032 coin cell or Swagelok type cells (see below). Hence the 18650 cells are specifically used to follow the pressure changes upon cycling.
The electrolyte solutions EC1 (comparative) and EC3 (invention) were implemented into a Na-ion 18650 cell (TIAMAT) composed of a Na3V2(PO4)2F3 cathode and a pre-sodiated hard carbon anode. The mass loading of the Na3V2(PO4)2F3 and hard carbon were exactly same as used for 2032 coin type cells, namely around 12 mg/cm2 for Na3V2(PO4)2F3 and around 6 mg/cm2 for hard carbon with positive to negative active material weight ratio of 2:1. The total amount of the active material used in 18650 cell is around 9.5 g of Na3V2(PO4)2F3 (around 15 mg in 2032coin cells). The positive and negative electrodes are coated on both sides of the Aluminium foil and they are wind together using Celgard separator to separate them physically. The winded electrodes with separator is then placed in cylindrical type cans with size of 18 mm diameter and 65 mm length and filled with electrolyte under study. Nearly 6 g of electrolyte is used for each cell and the can is sealed using a cap.
The pressure analyses in 18650 cells are carried out in home-made experimental set up where an optical fibre is placed in the 18650 cell that follow the pressure changes upon cycling. Cycling of charge and discharge was proceeded at 55° C. with a voltage range of 2.0 to 4.3 V.
The inventors measured the pressure inside the cell during the cycling, which is reported on
2. Analytical Data of Gaseous by-Product Formation
The inventors tested different combinations of additives and compared the level of gaseous by-product formation during cycling. To this aim, the electrolyte solutions EC1, EC2, EC3 and EC4 were used into home-made Swagelok type cells which were directly connected to a mass spectrometer in order to study all the formed gases. The positive and negative electrodes were self-standing film using polytetrafluoroethylene (PTFE) binder (10% by weight to a mixture of active material and conducting carbon in the ratio 85:15). The cells were cycled at C/10 rate (1C=128 mAh.g−1). The results of the electrochemical mass spectrometry analyses are represented on
Altogether,
To evaluate the wetting ability of the electrolyte, the contact angle measurements of the electrolyte EC3 on a three layers PP/PE/PP film (Celgard® separator) were performed by using KRUSS DSA 100 device within 10 seconds. Firstly, the PP/PE/PP separator was placed onto the glass subtract flatly. Then, 10 μL of electrolyte was placed onto the surface of separator. Lastly, the camera in the KRUSS DSA 100 device captures the image of the liquid onto the separator, and the contact angle was analysed.
Obviously, the EC3 can fully wet the PP/PE/PP separator.
Cylindrical type 18650 cells were assembled. For this purpose, dry cells (Reversible capacity 900 mAh, high energy cells) having Na3V2(PO4)2F3 (NVPF) and hard carbon (HC) as positive and negative electrode, respectively, were obtained from the company TIAMAT, France, and filled with the electrolyte composition EC12 (see example 1). The cell was used for high energy density.
The cell was cycled at 25° C. in 1C—1D (1C=128 mAh/g) rate within the potential window of 2-4.25 V. For every 10 cycles, the cycling rate was slowed down to a C/10: D/10 cycle in order to check the maximum available capacity in the cell. The capacity retention measured for 1C and C/10 are both shown in
The data observed in these 18650 cells using the electrolyte EC12 is in par with the results observed in coin cells. The 87% capacity retention (in C/10 cycling) after 2000 cycle shows the stability of the electrolyte EC12. Further no pressure raise is observed in the cell upon cycling and no current interruptive device (CID) break was observed.
Another 18650 dry cell, this time with relatively low loading electrodes (maximum reversible capacity: 700 mAh) was obtained from TIAMAT, France and filled with the EC 12 electrolyte composition. The cell was formulated at 55° C. for 2 cycles and then cycled at C/10 rate for 100 cycles at 55° C. to increase the degradations. After the high temperature cycling, the cell was brought to 25° C. and cycled at 1C-1D rate.
The initial 100 cycles were carried out in harsh condition (55° C. and slow rate—C/10) in order to promote electrolyte degradation. Still, as shown in
Electrolyte compositions according to the invention were prepared using the additive and salt of EC3 in the same relative quantity and a mixture of solvents which comprises methyl acetate (MA) at 4% or 20% (v/v based on the total volume of the solvent mix) as well as ethylene carbonate (EC), propylene carbonate (PC) and dimethyl carbonate (DMC). The respective volume ratios of the solvent mixtures are:
Impedance data were measured at 10° C., 25° C., 40° C. and 55° C. temperatures. The Impedance measurements were carried out in coin type 2032 cells using Na3V2(PO4)2F3 and hard carbon as positive and negative electrodes respectively. Biologic MPG-2 cycler integrated with impedance analyser is used for this purpose and measurements were carried using Potentio Electrochemical Impedance Spectroscopy (PEIS). A single sine input voltage signal of 10 mV sinus amplitude is used to probe the interphase and the output signal is measured. The frequency range of 10 kHz to 100 mHz is used for the analyses by recording 6 points per decade in logarithmic scale. Similar measurements were carried out for:
The resulting impedance graphs are shown in
In this example, the sodium salt is a mixture of NaPF6 and NaTFSI. The electrolyte composition corresponds to EC12 except for the presence of NaTFSI which is present in an amount of 3 wt. % based on the total weight of the electrolyte solvent and salt. Coin type cells were assembled using Na3V2(PO4)2F3 and hard carbon as positive and negative electrodes respectively. The cells were cycled at 55° C. and kept for self-discharge test at 55° C. in charged state for one week.
The solid line represents the (n−1)th cycle before self-discharge test, dotted line represents the discharge curve after self-discharge at 4.3 V (nth cycle) and the dashed line represent the recovery (n+1)th cycle, where n is 10. Almost 86.3% capacity of 9th cycle is retained after self-discharge at 4.3 V for one week and 95% capacity is recovered in the following recovery cycle.
As shown, the capacity recovery after self-discharge is 95%, this indicating that NaTFSI can be added as additional salt in the proposed electrolyte combination.
| Number | Date | Country | Kind |
|---|---|---|---|
| 21305354.9 | Mar 2021 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2022/057478 | 3/22/2022 | WO |
