WO2011113111A1 - Ionic liquids for batteries - Google Patents
Ionic liquids for batteries Download PDFInfo
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- WO2011113111A1 WO2011113111A1 PCT/AU2011/000308 AU2011000308W WO2011113111A1 WO 2011113111 A1 WO2011113111 A1 WO 2011113111A1 AU 2011000308 W AU2011000308 W AU 2011000308W WO 2011113111 A1 WO2011113111 A1 WO 2011113111A1
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- organic cation
- electrolyte
- battery
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- ionic liquid
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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
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D498/00—Heterocyclic compounds containing in the condensed system at least one hetero ring having nitrogen and oxygen atoms as the only ring hetero atoms
- C07D498/02—Heterocyclic compounds containing in the condensed system at least one hetero ring having nitrogen and oxygen atoms as the only ring hetero atoms in which the condensed system contains two hetero rings
- C07D498/10—Spiro-condensed systems
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0568—Liquid materials characterised by the solutes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0569—Liquid materials characterised by the solvents
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention relates to room temperature ionic liquids suitable for use in batteries.
- the invention is particularly suitable for application in lithium batteries.
- a species is reduced at one electrode (ie gains electrons) and then oxidised at another electrode (ie loses electrons).
- the species being reduced / oxidised may be present in the electrolyte solution that connects the 2 electrodes, or may be present in the electrodes themselves, or may be from an external source.
- both the electrolyte and the electrodes are involved in the electrochemical reaction.
- the Co transition metal in the Oathode is reduced (Co 4+ - Co 3+ ) and Li + is extracted from the anode (Li x C 6 - xLi + + 6C + xe " ), which is also known as dedoping or deintercalation, and inserted into vacancies in the cathode (Li -x Co02 + xLi + + xe ' -> LiCo0 2 ), which is also known as doping or intercalation.
- cathode is oxidised (Co 3+ ' - Co 4+ ) and Lf is extracted from the cathode (LiCo0 2 -> Lii. x Co0 2 + xLi + + xe " ) and inserted into the anode (xLf + 6C + xe " -> LixCe).
- cathode materials which generally have the form LiM x O y where is at least one element selected from the group consisting of Co, Ni, Mn, Fe, Al, V and Ti (such as LiMn0 2 , LiFeP0 4 and Li 2 FeP0 4 F).
- the net electromotive force is the sum of the Chemical EMF (ie the reduction / oxidation reactions during discharging), and any voltage difference EMF applied across its terminals (ie during charging).
- EMF electromotive force
- the chemical EMF is the difference between the reduction potentials of each electrode.
- the reduction potential at the anode and cathode are measured relative to a reference electrode and the reduction potential of the cell, expressed by reference to the cathode, is the difference between these 2 values.
- the reduction potential of the cell for LiCo0 2 is about 3.7 V
- for LiMn0 2 is about 4.0 V
- for LiFeP0 is about 3.3 V
- for Li 2 FeP0 4 F is about 3.6 V.
- the EMF may also be referred to as the discharge voltage.
- Aprotic electrolytes for example those based on compounds such as ethylene carbonate or propylene carbonate and mixtures thereof, are often employed as the electrolyte.
- these compounds have low boiling and flash points, are electrochemically unstable (ie they degrade / decompose at the electrodes which inhibits current flow), and they can be toxic.
- these electrolytes normally require the doping with a corrosive lithium salt, such as lithium hexafluorophosphate (LiPF 6 ), lithium tetrafluoroborate (LiBF 4 ), and lithium perchlorate (LiCI0 4 ).
- a corrosive lithium salt such as lithium hexafluorophosphate (LiPF 6 ), lithium tetrafluoroborate (LiBF 4 ), and lithium perchlorate (LiCI0 4 ).
- HF hydrofluoric acid
- HCI hydrochloric acid
- Ionic liquids have the ability to act as both solvents and electrolytes for electrochemical devices.
- ILs are salt compositions (ie mixtures of cations and anions) that are molten at the temperature of interest.
- Room temperature ionic liquids (RTILs) are thus salt compositions that are molten at room temperature.
- Room temperature as used herein is taken to include the range of commonly experienced ambient temperatures rather than the scientific definition. For instance, room temperature is to be taken to be the temperature range from about 0 °C to about 100 °G.
- RTILs have been used as electrolytes in electrochemical cells (eg batteries), capacitors, photochemical cells, electroplating, electrorefining, catalysis and synthesis.
- the below discusses the operation within a lithium ion battery.
- Li + moves from the positive electrode to the negative anode.
- Achieving the high EMFs (above about 3 V) is dependent on movement of charged species between the electrodes, which in turn is dependent on the properties of the electrolyte.
- the properties of the electrolyte must be such that the following problems are avoided: (1) generation of a solid electrolyte interface (SEI) layer at the negative anode that is impermeable to Li + , and (2) inhibition of the migration of Li + through the electrolyte from the positive cathode to the negative anode by clustering of negative ions around the positive Li + ion.
- SEI solid electrolyte interface
- the SEI forms on the electrodes of a battery via decomposition products of the electrolyte and/or additives during the initial cycling of the device. Stabilizing the SEI serves to protect the bulk electrolyte from further decomposition. By controlling the composition, thickness and uniformity of this layer several battery properties can be improved including reducing the internal resistance of the cell, which in turn reduces self-discharge, and improvements in cell cycling efficiency.
- lithium salt substantially changes some of the physical properties of the electrolyte, including increasing the viscosity and decreasing the ionic conductivity, due mainly to strong ion-ion interactions. These strong interactions, especially between Li+ and the anion(s) of the IL electrolyte, can 'bind' lithium into charged clusters. These clusters are negatively charged (due to the preponderance of anions) and will thus want to migrate (the Li+) in the opposite direction to which we wish them to migrate (the Li+) under both charge and discharge. This leads to low diffusivity of the Li+ and low transport numbers (t L i+), within the bulk electrolyte.
- lithium battery is intended to encompass both lithium metal and lithium ion batteries. Therefore, the invention is directed towards overcoming one or both of these existing problems of the electrolyte.
- an electrolyte when used in a battery including a first organic cation, the first organic cation including, consisting essentially of or consisting of a heteroatom-containing cyclic compound having (i) at least 2 ring structures that share at least one common atom, the cyclic structure having and (ii) both a formal positive charge of at least +1 and a partial negative charge.
- the cyclic compound may include rings joined at a single atom (termed herein spirocyclic rings), rings fused at adjacent atoms (termed herein fused rings), or bridging rings joined by non-adjacent atoms (termed herein bridgehead rings).
- the cyclic compound has at least 2 ring structures (termed herein bicyclic) or may have more that 2 ring structures; for instance, 3, 4 or 5 rings.
- the first organic cation and a first anion form a first ionic liquid.
- the electrolyte may include, consist essentially of, or consist of the first organic cation and a first anion as an ionic liquid.
- the electrolyte further includes a second ionic liquid having a second organic cation and a second anion.
- the structure of the second organic cation need not be the same as that of the first organic cation described herein, and instead may be any ionic liquid organic cation known in the art.
- the second organic cation may be any known in the art, for instance, imidazolium (eg 1 -ethyl-3- methylimidazolium (EMI)), pyrrolidinium or morpholinium or derivatives thereof.
- the first and second anions may also be any known in the art, for instance, hexafluorophosphate (PF 6 ), tetrafluoroborate (BF 4 ), perchlorate (CI0 4 ), bis(fluorosulfonyl)imide (FSI) or bis(trifluoromethanesulfonyl)imide (TFSI) or derivatives thereof.
- the first organic cation may be used as a dopant to the second ionic liquid, or the electrolyte may include, consist essentially of, or consist of both the first ionic liquid and the second ionic liquid.
- the amount of the first organic cation as a percentage of the total organic cation may be from about 1% to about 99%.
- the battery may be an alkali-metal battery, such as a lithium battery (eg lithium metal or lithium ion), or a transition metal battery.
- the battery is a lithium metal or lithium ion battery. More preferably, the battery is a lithium metal battery.
- the electrolyte may further include a metal salt.
- a metal salt is a lithium salt including a Li cation.
- the chemical nature of the first organic cation is such that it is at least partially attracted or weakly bound to the Li cation of the lithium battery. That is, the first organic cation is such that it coordinates or interacts with the Li cation of the lithium battery.
- the desirable degree of such interaction will depend on the application, but will be that which results in the requisite balance between (i) interacting sufficiently strongly to shield or destabilise the Li cation from the stronger interaction with the anion of the electrolyte (eg the first or second anion) and (ii) interacting sufficiently weakly to allow the Li cation to interact at the electrodes.
- the partial negative charge Of the first organic cation coordinates or interacts with the Li cation.
- the formal positive charge and the partial negative charge are separated such that the first organic cation has a net dipole.
- the formal positive charge may be present on an opposite portion of a ring to the partial negative charge.
- the formal positive charge may be present on a different ring to the partial negative charge.
- the formal positive charge is present on or near the portion that is between 2 rings. That is, the formal positive charge may be the spiro atom, or one of the joining atoms in a fused ring.
- a . positive functional group provides the formal positive charge by including a first element from Group 15 of the Periodic Table of the Elements.
- first element participates in, or forms, 4 covalent bonds in the first organic cation iuch that a formal positive charge results.
- the first element is N or P.
- a positive functional group may contain more than one first element, which may be the same or different.
- a negative functional group provides the partial negative charge by including a second element.
- the second element participates in, or forms, covalent bonding such jthat a partial negative charge results. That is, the second element participates in; or forms, covalent bonding such that a lone electron pair results.
- the second element may be the relatively electronegative elements O, S, N or F.
- a negative functional group may contain more than one second element, which may be the same or different.
- a battery including at least one anode and at least one cathode; and an electrolyte for fluid communication between the anode and cathode; the electrolyte including a first organic cation, the first organic cation including, Consisting essentially of or consisting of a heteroatom-containing cyclic compound having at least 2 ring structures that share at least one common atom, the cyclic structure having a formal positive charge of at least +1 and a partial negative charge.
- a first organic cation including, consisting essentially of . or consisting of a heteroatom-containing cyclic compound having at least 2 ring structures that share at least one common atom, the cyclic structure having a formal positive charge of at least +1 and a partial negative charge.
- the first organic cation is as according to the above description.
- an ionic liquid including an organic ciation including, consisting essentially of or consisting of a heteroatom-containing cyclic compound having at least 2 ring structures that share at least one common atom, the cyclic structure having a formal positive charge of at least +1 and a partial negative charge.
- the first organic cation is as according to the above description.
- an ionic liquid including, consisting Essentially of or consisting of a heteroatom-containing cyclic compound having at least
- the cyclic structure having a formal positive charge of at least +1 and a partial negative charge wherein the ionic liquid is such that use of the ionic liquid in the battery results in the formation of an appropriate SE ⁇ .
- the first organic cation is as according to the above description.
- the organic cation can be used as electrolyte in a battery or as an additive to an ionic liquid or carbonate based solvent electrolytes. If the organic cation is used as an additive it can be in the , concentration of 0.1 to 1.5 mol/kg with the preferred concentration being 0.25 mol/kg.
- the ionic liquid can be made using the organic cation or can be any previously described ionic liquid for example those based on pyrrolidinium or imidazolium cations with TFSA, FSA, DCA, BF4 or PF 6 anions
- the concentration of lithium ions in the electrolyte can be in the range of 0.1 to 1.5 mol/kg with the preferred concentration being 0.5 mol/kg.
- the battery separator can be any commercially available separator. Brief description of the figures
- Figure 1 The Spiro-based compound whose electrochemistry is described in Figures 2,
- A is the ionic liquid cation of the invention.
- B is an ionic liquid anion.
- FIG. 2 shows an energy storage device in accordance with one embodiment of the present invention
- Figure 3 Electrochemical window of the SMK TFSA ionic liquid without lithium salt. The oxidation peaks at -1 and 0 volts are a result of the oxidation of products formed during the reductive decomposition seen negatively beyond -2 V. They do not relate to the neat i ⁇ >nic liquid. Platinum has been used as both the counter and working electrodes and Ag
- Figure 4 Lithium cycling in the SMK TFSA 0.4 mol/kg LiTFSA. Note the lack of breakdown current until -6 V on the first scan, and the stabilisation of the current behaviour after the 2nd scan. Pt counter and working electrodes and Ag
- Figure 5 Lithium cycling of a lithium: lithium symmetrical cell containing SMK TFSA 0.4 mol/kg LiTFSA at a current density of 0.1 mA.cm "2 and 85 °C.
- FIG. 7 A lithium metal battery comprising LiFeP0 4 cathode (2.2 mg.cm "2 loading), Separion separator and an electrolyte consisting of C 3 mpyr TFSA with 0.25 mol/kg SMK TFSA and 0.5 mol.kg '1 LiTFSA as the electrolyte.
- the cell was charged at 0.05 mA.cm “2 (C/7.5) and discharged at 0.1 mA.cm "2 (C/3.75) at 50 °C.
- FIG. 8 A lithium metal battery comprising a LiFeP0 4 cathode (1.5 mg.cm '2 loading), sepafion separator and ah electrolyte consisting of C 3 mpyr TFSA with 0.25 mol/kg SMK TFSA and 0.5 mol/kg LiTFSA. The cell was charged at a rate of C/10 and discharged at a rate of C/10 at 80 °C.
- FIG. 9 A lithium metal battery comprising a LiFeP0 4 cathode (1.5 mg.cm "2 loading), Separion separator and an electrolyte consisting of C 3 mpyr TFSA with 0.25 mol/kg SMK TFSA and 0.5 mol/kg LiTFSA. The cell was charged at a rate of C/10 and discharged at a rate of C/10 at 115 °C.
- Figure 10 Lithium metal batteries comprising a LiFeP0 cathode (1.5 mg.cm "2 loading), an electrolyte consisting of C 3 iripyr TFSA with 0.25 mol/kg SMK TFSA and 0.5 mol/kg LiTFSA.
- the cells were charged at a rate of C/10 and discharged at a rate of C/10 at 80 "jC.
- the first cell uses a Separion separator (open circles)
- the second cell uses a PVdF Separator (filled triangles)
- the third cell uses a poly(acrylonitrile) (PAN) separator (crosses)
- FIG 11 A lithium metal battery comprising a LiFeP0 4 cathode (1.5 mg.cm "2 loading), PVdF separator and an electrolyte consisting of Campyr TFSA with 0.25 mol/kg SMK TFSA and 0.5 mol/kg LiTFSA. The cell was charged at a rate of C/10 and discharged at a rate of C/10 at 120 °C.
- the first organic cation of the present invention has the general structure given in Formula 1 :
- rings A and B are 5- or 6-membered rings. However, smaller and larger rings may be suitable for application in a lithium battery as could be determined by the skilled person.
- Rings A and/or B include
- X1 is the first element providing the first organic cation with a formal positive charge.
- X1 may be considered to be a positive functional group.
- X1 may be selected from the group consisting of N, P, As, Sb or Bi.
- X1 is N.
- the formal positive charge is provided elsewhere than X1 ; and
- a negative functional group including one or more electronegative heteroatoms (the 'second element') providing the first organic cation with a partial negative charge.
- the heteroatom may be selected from the group consisting of O, N or S.
- An advantage of having the reductively vulnerable quaternary N at the X1 position of a spiro compound is that it will be better protected (sterically) from the cathode surface by the A and B rings. This protection will result in increased reductive stability of the cation, which is particularly important at deeply negative potentials such as those present in lithium batteries.
- the first organic cation may include more than one negative functional group, or more than one second element within the negative functional group.
- the second element may be strictly part of ring A and/or B, or may be appendant to ring A and/or B.
- the first organic cation includes a single positive functional group or first element.
- Rings A and/or B may further include groups selected from lactone, amide, anhydride, carbonate, carbonyl, sulphate, sulphonate, phosphate or phosphonate.
- Rings A and/or B may be further substituted, preferably with groups having an electron donating function.
- rings A and/or B may be substituted by alkoxide, nitro, amino, amides, esters, and alkenes.
- Rings A and/or B may also be substituted by alkanes, for example, ring A and/or B may be substituted by alkyl groups (for instance, methyl, ethyl, propyl, and ⁇ -Bu alkyl groups).
- the alkyl groups may have a linear chain length of from about 1 to about 12 atoms.
- the alkyl groups may have a linear chain length of from about 1 to about 8 atoms.
- X1 is two or more atoms that join rings A and B.
- X1 is 2 atoms.
- rings A and B may be fused or bridged, and X1 may be C, O, N and B atoms.
- the carbon atoms may be bonded to each other via alkyl or alkenyl bonds.
- X1 is not the first element providing the first organic cation with a formal positive charge, which is provided elsewhere than X1 in rings A and/or B.
- Rings A and B are, in some further embodiments, attached to one or more additional rings of the type A or B as discussed above, as shown in Formula 2:
- X2 has the characteristics defined for X1 above.
- the first element typically provides a formal positive charge of +1.
- the negative functional group typically provides a partial negative charge by either (i) possessing a lone electron pair and the subsequent in resonance / derealization effect, or (ii) an inductive effect.
- Examples of (i) include carbonyl functional groups.
- Examples of (ii) include ether functional groups.
- the first organic cation when present as a sole dopant or as part of an ionic mixture (ionic liquid), is typically not a liquid at room temperature.
- the electrolyte in order to be used in a lithium battery, the electrolyte must be fluid enough to allow the migration of Li ions.
- the first organic cation needs to be mixed with other components to cause it to be - a room temperature liquid.
- the first organic cation may be mixed with any other suitable room temperature liquid (either ionic or aprotic).
- any other suitable room temperature liquid either ionic or aprotic.
- adding, for instance, carbonyl or methyl groups to a compound would disrupt the order and may lead to a liquid material at room temperature.
- first organic cations having negative functional groups of varying negativity could be obtained.
- a negative functional group including an O atom as the second element for instance in a morpholinium ring
- the S will have two lone electron pairs, which will contribute to a strong ⁇ " charge and the ability to more strongly complex with Li ion.
- S is also larger than O and will therefore have a more diffuse partial negative charge resulting in a weaker Li interaction.
- a negative functional group that is a carbonyl group will be more negative than a functional group that is an ether group.
- the appropriate negativity of the negative functional groups of the first organic cation is dependent on the application. For instance, a battery involving a Li ion (valence +1) would need to be coordinated by a weaker negative functional group on the first organic cation than would say a battery involving a Mg ion (valence +2), Na ion (valence +2), or Al ion (valence +3). Further, depending on the application, the electrolyte needs to be of a certain 'robustness' so that generation of the SEI is optimal (ie not too little and not too much).
- compounds having two or more negative functional groups may potentially co-ordinate two or more Li ions per first organic cation, or with a single Li ion more strongly, depending on the positioning of the negative functional groups in the first organic cation.
- the first organic cation when used as part of an ionic liquid, could be used together with any ionic liquid anion known to those skilled in the art.
- Suitable examples of anions are as follows:
- bis(trifluoromethylsulfonyl)imide (the term “amide” instead of “imide” is sometimes used in the scientific literature and is used interchangeably in the literature and herein to essentially refer to the same anion with the same characteristics) and is abbreviated to TFSA, TFSI or N(Tf) 2 or another of the sulfonyl imides, including the bis imides and perfluorinated versions thereof.
- This class includes (CH3S02)2 ⁇ . (CF3S02)2 " (also abbreviated to Tf 2 N), (FS0 2 ) 2 " and (C 2 F 5 S0 2 ) 2 N " as examples.
- Halides alkyl halides or perhalogenated alkyl halides of group VA(15) elements.
- E is P or Sb.
- this class encompasses PF 6 " , SbF 6 " , P(C 2 F 5 )3F3-, Sb(C 2 F 5 ) 3 F 3 -, P(C 2 F 5 )4F 2 ' , AsF 6 " , P(C 2 H 5 ) 3 F 3 - and so forth;
- sulfonyl and sulfonate compounds namely anions containing the sulfonyl group 4 S0 2 , or sulfonate group S0 3 " not covered by groups (i) and (iv) above.
- This class encompasses aromatic sulfonates containing optionally substituted aromatic (aryl) groups, such as toluene sulfonate and xylene sulfonate;
- Weak base anions being the weakly basic anions, such as Lewis base anions, including lactate, formate, acetate, carboxylate, dicyanamide, hexafluorophosphate, bis(trifluoromethanessulfonyl)amide, tetrafluoroborate, methane sulfonate, thiocyanate, tricyanomethide and tesylate;
- Lewis base anions including lactate, formate, acetate, carboxylate, dicyanamide, hexafluorophosphate, bis(trifluoromethanessulfonyl)amide, tetrafluoroborate, methane sulfonate, thiocyanate, tricyanomethide and tesylate;
- the preferred classes are those outlined in groups (i), (ii), (iii), (iv) and (vi) above, and particularly group (i).
- alkyl is used in its broadest sense to refer to any straight chain, branched or cyclic alkyl groups of from 1 i
- the alkyl group is preferably straight chained.
- the alkyl chain may also contain hetero-atoms, a halogen, a nitrile group, and generally other groups or ring fragments consistent with the substituent promoting or supporting electrochemical stability and conductivity.
- Halogen, halo, the abbreviation "Hal” and the like terms refer to fluoro, chloro, bromo and ipdo, or the halide anions as the case may be.
- the 2-oxo-3,9-dioxa-6-azoniaspiro[5.5]undecane bis(tr ' ifluoromethylsulfonyl)amide defined herein as [SMKJfTFSA] was prepared from 2-oxo-3,9-dioxa-6- azoniaspiro[5.5]undecane bromide [SMK][Br] (5.91 g, 23.5 mmol) and LifTFSA] (6.74 g, 23.5 mmol) were each dissolved in 150 mL water. After combining the two solutions Ijhe biphasic reaction mixture was heated until a homogeneous solution was formed. After cooling to 5 °C for 24 h the colourless, crystalline product was filtered and washed with 5 °C water. Yield 2.92 g (27.5 %).
- Figure 5 shows a lithium: lithium symmetrical coin cell (CR2032) cycling results using Separion as the separator with the SMK TFSA 0.4 mol.kg "1 LiTFSA as the electrolyte, the cell was cycled at 0.1 mA.cm "2 and 85 °C as the electrolyte is a liquid at this temperature.
- the increasing polarisation of this cell with increasing cycle number which is caused by the high viscosity of the solution at this temperature slowing the lithium ion motion.
- a secondary lithium battery (1) produced in accordance with the invention is shown Schematically in Figure 2.
- This battery comprises a case (2), at least one positive electrode (3) (one is shown) comprising lithium iron phosphate, at least one negative electrode (4) (one is shown) an ionic liquid electrolyte comprising an anion and a cation counterion and a lithium salt (5), a separator.(6) and electrical terminals (7,8) extending from the case (2).
- the battery (1) illustrated is shown in plate-form, but it may be in any other form known in the art, such as spiral wound form.
- the electrolyte is prepared by adding 0.25 mol/kg of SMK TFSA to C 3 mpyrTFSA and stirring until the solid is dissolved. To this 0.5 mol/kg of LiTFSA is added with further stirring until solid is dissolved. All additions are performed in a high purity argon glovebox and the final electrolyte mixture contains 35 ppm of water. All batteries whose data is shown in figures 8 to 11 have been constructed by the following method.
- the anode consists of a lithium metal foil which has been cleaned by washing in hexane and scrubbed to remove surface impurities.
- the cathode consists of a LiFeP0 4 active material with Shawinigan black carbon additive and PVdF binder at ratios of 75:15:10.
- the cathode loading is 1.5 mg.cm "2 .
- the anode is cut to a 13 mm diameter disc while the cathode is cut to a 13 mm diameter disc.
- the separator is cut to a 15 mm disc. All the electrodes and separator are stacked into a CR2032 coin cell containing a Teflon gasket and 70 ⁇ _ of electrolyte solution is added. The CR2032 coin cell is then sealed using a commercially available coin cell press.
- the prepared batteries are then stored at the operating temperature used for the cycling measurements for 12 hours prior to cycling. All cycling has been performed at a charge rate of C/10 and a discharge rate of C/10.
- the optimal electrolyte mixture was determined from successive experiments by varying the concentration of SMK TFSA in the host ionic liquid C 3 mpyr TFSA in steps of 0.1, 0.25, 0.5 and 1 mol.kg "1 while maintaining the lithium salt concentration at 0.5 mol.kg “1 in the final electrolyte.
- Figure 7 shows that at a concentration of 0.25 mol.kg “1 , the SMK TFSA stabilises the battery capacity at -130 mAh.g "1 at 50 °C.
- Example 4 Battery cycling at 80 °C
- SMK TFSA is used as an additive to the C 3 mpyr TFSA ionic 1 liquid electrolyte as described earlier.
- Figure 8 shows the battery cycling at a rate of C/10 charge and C/10 discharge and plotted is the discharge capacity and shows that the SMK TFSA can stabilise cycling at 80 °C using a commercially available Separion separator.
- the figures shows that a stable capacity of -105 mAh/g is achieved using SMK TFSA as an additive
- a battery was prepared whereby SMK TFSA is used as an additive to the C 3 mpyr TFSA ionic liquid electrolyte as described earlier.
- Figure 9 shows the battery cycling at a rate of C/10 charge and C/10 discharge and plotted is the discharge capacity and shows that the SMK TFSA can stabilise cycling at 115 °C using a commercially available Separion separator. The figure shows that at the higher temperature the battery operates better and the decay in discharge capacity is not as significant as at lower temperature. The figure also shows a stable capacity of ⁇ 160 mAh/g is achieved using SMK TFSA as an additive which is a higher value then for 80 °C.
- SMK TFSA is used as an additive to the C 3 mpyr TFSA ionic liquid electrolyte as described earlier.
- the first battery contains the Separion separator
- the second battery contains a modified PVdF separator
- the third battery contains .a PAN (polyacrylonitrile).
- Figure 10 shows the battery cycling at a rate of C/10 charge and C/10 discharge and plotted is the discharge capacity (data for the battery with Separion separator is open circles, for the battery with PVdF separator is filled triangles and for the battery with PAN separator is crosses).
- Figure 9 shows that the battery containing the modified PVdF separator and SMK TFSA additive stabilises battery cycling compared to batteries containing Separion and SMK TFSA additive or PAN separator and SMK TFSA additive at 80 °C.
- Example 7 Battery cycling at 120 °C
- SMK TFSA is used as an additive to the C 3 mpyr TFSA ipnic liquid electrolyte as described earlier.
- Figure 11 shows the battery cycling at a rate of C/10 charge and C/10 discharge and plotted is the discharge capacity and shows that the SMK TFSA can stabilise cycling at 120 °C when using a modified PVdF separator.
- the figure also shows a stable capacity of -160 mAh/g is achieved using SMK TFSA as an additive and the PVdF seperator
- electrolytes including the organic cation of the invention and particularly SMK, anion and metal salt can show stable cycling at operating temperatures up to 200°C.
- These batteries will have application in high temperature environments and may be particularly suited to use in sensors and monitoring equipment such as those found in the oil and gas industry.
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Abstract
Description
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Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP11755571.4A EP2548258A4 (en) | 2010-03-18 | 2011-03-18 | Ionic liquids for batteries |
CN201180013903.8A CN102971902B (en) | 2010-03-18 | 2011-03-18 | For the ionic liquid of battery |
US13/635,825 US20130202973A1 (en) | 2010-03-18 | 2011-03-18 | Ionic liquids for batteries |
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AU2010901143 | 2010-03-18 | ||
AU2010901143A AU2010901143A0 (en) | 2010-03-18 | Ionic liquids for batteries |
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WO2011113111A1 true WO2011113111A1 (en) | 2011-09-22 |
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PCT/AU2011/000308 WO2011113111A1 (en) | 2010-03-18 | 2011-03-18 | Ionic liquids for batteries |
Country Status (4)
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US (1) | US20130202973A1 (en) |
EP (1) | EP2548258A4 (en) |
CN (1) | CN102971902B (en) |
WO (1) | WO2011113111A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140099529A1 (en) * | 2012-10-05 | 2014-04-10 | Semiconductor Energy Laboratory Co., Ltd. | Power storage device |
Families Citing this family (5)
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US10707526B2 (en) | 2015-03-27 | 2020-07-07 | New Dominion Enterprises Inc. | All-inorganic solvents for electrolytes |
WO2017173323A1 (en) | 2016-04-01 | 2017-10-05 | NOHMs Technologies, Inc. | Modified ionic liquids containing phosphorus |
US10707531B1 (en) | 2016-09-27 | 2020-07-07 | New Dominion Enterprises Inc. | All-inorganic solvents for electrolytes |
CA3069973A1 (en) | 2017-07-17 | 2019-01-24 | NOHMs Technologies, Inc. | Phosphorus containing electrolytes |
US11267707B2 (en) | 2019-04-16 | 2022-03-08 | Honeywell International Inc | Purification of bis(fluorosulfonyl) imide |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02181413A (en) * | 1989-01-06 | 1990-07-16 | Nippon Chemicon Corp | Electrolyte for electrolytic capacitor |
WO2004082059A1 (en) * | 2003-03-13 | 2004-09-23 | Commonwealth Scientific And Industrial Research Organisation | Energy storage devices |
JP2005175239A (en) * | 2003-12-12 | 2005-06-30 | Japan Carlit Co Ltd:The | Electric double-layer capacitor and electrolyte thereof |
JP2005222973A (en) * | 2004-02-03 | 2005-08-18 | Japan Carlit Co Ltd:The | Electrolyte for electric double-layer capacitor, and the electric double-layer capacitor |
Family Cites Families (2)
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JP2002181413A (en) * | 2000-12-12 | 2002-06-26 | Matsushita Electric Ind Co Ltd | Method for manufacturing refrigerating-cycle constituting body |
EP1919922B1 (en) * | 2005-08-30 | 2011-04-20 | Honeywell International Inc. | Method for synthesizing spiro quaternary ammonium systems |
-
2011
- 2011-03-18 US US13/635,825 patent/US20130202973A1/en not_active Abandoned
- 2011-03-18 CN CN201180013903.8A patent/CN102971902B/en not_active Expired - Fee Related
- 2011-03-18 EP EP11755571.4A patent/EP2548258A4/en not_active Withdrawn
- 2011-03-18 WO PCT/AU2011/000308 patent/WO2011113111A1/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02181413A (en) * | 1989-01-06 | 1990-07-16 | Nippon Chemicon Corp | Electrolyte for electrolytic capacitor |
WO2004082059A1 (en) * | 2003-03-13 | 2004-09-23 | Commonwealth Scientific And Industrial Research Organisation | Energy storage devices |
JP2005175239A (en) * | 2003-12-12 | 2005-06-30 | Japan Carlit Co Ltd:The | Electric double-layer capacitor and electrolyte thereof |
JP2005222973A (en) * | 2004-02-03 | 2005-08-18 | Japan Carlit Co Ltd:The | Electrolyte for electric double-layer capacitor, and the electric double-layer capacitor |
Non-Patent Citations (10)
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140099529A1 (en) * | 2012-10-05 | 2014-04-10 | Semiconductor Energy Laboratory Co., Ltd. | Power storage device |
TWI627780B (en) * | 2012-10-05 | 2018-06-21 | 半導體能源研究所股份有限公司 | Power storage device |
Also Published As
Publication number | Publication date |
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US20130202973A1 (en) | 2013-08-08 |
EP2548258A1 (en) | 2013-01-23 |
CN102971902B (en) | 2015-10-07 |
EP2548258A4 (en) | 2013-08-07 |
CN102971902A (en) | 2013-03-13 |
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