The present invention relates to novel electrode materials for Li-based electrochemical energy storage devices and to a Li-based electrochemical storage device.
Lithium batteries are known in non-rechargeable and in rechargeable form. Such batteries comprise positive and negative electrodes with a non-aqueous electrolyte disposed between them. In a rechargeable lithium ion battery (secondary battery) the positive electrode of the battery can for example be LiCoO2 (referred to as the “cathode” in Li-battery community) and the negative electrode can for example be carbon (referred to as the “anode” in Li-battery community). In a non-rechargeable battery (primary battery) the positive electrode can for example be MnO2 and the negative electrode can be lithium metal.
In the state of the art, lithium-ion batteries and RuO2 proton-type super-capacitors are used for rechargeable electrochemical storage devices. Among current commercial Li-ion batteries, when carbon is used as an anode material, the Li-storage capacity is less than 372 mAh/g. When LiCoO2 is used as the cathode material it has a capacity less than 150 mAh/g. For RuO2 proton-type supercapacitors, the highest capacitance is reported as 1200 F/g, less than 200 mAh/g.
Various different types of electrolyte are known. For example there is the class of liquid electrolytes comprising at least one ionically conducting salt such as Li(TFSI), i.e. lithium bis(trifluorosulphonyl)imide, LiPF6, i.e. lithium hexafluorophosphate or LiClO4, i.e. lithium perchlorate which are present, with a low degree of association, within a non-aqueous solvent such as a mixture of DME (dimethylethane) and EC (ethylene carbonate), a mixture of DEC (diethylene carbonate) and EC, or a mixture of DMC (dimethyl carbonate) and EC or PC (propylene carbonate) or combinations thereof.
In addition there are so-called dry polymer electrolytes. In these electrolytes the salt is selected as before (i.e. for example from Li(TFSI), LiPF6 or LiClO4) and is dispersed in a polymer or mixture of polymers. Suitable polymers comprise PEO (polyethylene oxide), PVDF (polyvinylene difluoride), PAN (polyacrylonitrile), and PMMA (polymethyl methyl acrylate).
Furthermore, there are so called polymer gel electrolytes. These have the same basic composition as the dry polymer electrolytes recited above but include a solvent, for example a solvent of the kind recited in connection with the liquid electrolytes given above.
The known liquid electrolytes described have the advantage that they have a high ionic conductivity up to a transference number of 0.6 and a high conductivity of 10−2 S/cm. In addition the liquid properties ensure good wetting of the electrode surface. They are however dangerous because leakage can occur, so that safety considerations arise. In addition they can lead to passivation effects which are undesirable.
The dry polymer electrolytes do not result in good wetting of the electrodes, the conductivities which can be achieved are quite low and there is also not much scope for modifying the chemical composition of the ingredients. However, the electrolytes are good safety-wise and no leakage occurs.
With the polymer gel electrolytes the change in liquid content results in reductions in the conductivity and there is also the danger of leakage.
An improved electrolyte is described in European patent application 03018161.4 filed on Aug. 8, 2003 and assigned to the present applicants, the content of this application is hereby incorporated into the present application by reference. In accordance with the above referenced European application there is provided:
a non-aqueous electrolyte including
It has namely been found that the addition of fine oxide particles, e.g. in powder or elongate particle form, leads to a substantial increase in conductivity but with no disadvantages.
The electrolyte preferably has a low degree of dissociation, preferably with an association constant in the range from 1×10−1 to 108/l−.mol−1.
When used in a primary or secondary lithium battery having positive and negative electrodes, the oxide should be selected such that it does not react with the material of either of said positive and negative electrodes.
The non-aqueous electrolyte described in the above referenced European application is not restricted to use in a battery, it can for example be used in a supercapacitor, in electrochromic devices such as electro-chromic displays or in a solar energy cell.
In the non-aqueous electrolyte described in the European application the ionically conductive salt is selected from the group comprising Li(TFSI), LiPF6 and LiClO4.
Moreover, the non-aqueous, anhydrous solvent is preferably selected from the group comprising DEC/EC, DMC/EC, PC, carbonate based solvents related to any of the foregoing, DMSO, organic sulphur compounds, THF, AN and mixtures of any of the foregoing.
The oxide used is preferably selected from the group comprising oxides exhibiting acidic properties, for example SiO2, TiO2 and oxides exhibiting basic properties, for example Al2O3, MgO and any mixtures thereof.
The average particle size of the oxide for particles of approximately spherical shape, is selected to be less than 5 μm and preferably less than 2 μm, with no lower limit other than that set by manufacturing techniques used to produce said oxide. For elongate particles, such as nano-wires or nano-tubes, the average diameter is selected to be less than 1 μm, preferably less than 100 nm, there being no limit on the length of such elongate particles.
The amount of oxide present in the electrolyte is preferably such as to give the electrolyte a consistency between that of a liquid and a solid, preferably a consistency similar to that of a soggy sand, i.e. a liquid and sand mixture having a consistency such that sedimentation effects do not occur.
The above electrolytes can all be used with the electrodes and in the electrochemical storage device of the present invention.
Due to the rapid development of the electronic industries, there is a great demand to increase further the energy density of electrochemical energy storage devices, leading to great interest in novel electrode materials.
Accordingly, the object of the present invention is to provide novel materials which permit a significant improvement in the electrochemical performance of Li-based electrochemical energy storage devices and electrodes for such Li-based electrochemical energy storage devices.
In order to satisfy this object, there are provided, in accordance with the invention, the electrodes of claims 1, 4 and 5 and 6 and the Li-based electrochemical storage device of claims 7 and 8.
The applicants have namely found that the transition metal halides, in particular the fluorides, and also ruthenium and molybdenum oxides can be used for Li-based electrochemical energy storage devices over a wide voltage range, for example from 0 to 4.3 V, and that they show large Li-storage capacities and good cyclic performance.
Furthermore, it has also been found that amorphous composites consisting of metal clusters of a transition metal and Li2O or LiF dispersed at an atomic scale or at a nanometer scale also show high reversible Li-storage behaviour.
More specifically, the following advantages can be achieved:
When the transition metal fluorides (the metal comprising one or more of the transition metals Ti, V, Cr, Ni, Mn, Fe, Co, Cu) is used as an active electrode material in an Li-based electrochemical energy storage device, high reversible capacities >500 mAh/g and sufficient cyclic performance over a wide voltage range, typically from 0-4.3V are achieved. Some transition metal fluorides show high voltage as high as 3.5 V, such as CoF3 and CuF2.
Furthermore, it has been found that ruthenium and molybdenum oxides can be used as electrode materials for Li-based electrochemical energy storage devices and that these exhibit very high capacities, for example 1200 mAh/g, high Coulombic efficiency (typically about 100%), good reversibility over a wide voltage range (typically 0-4.3V) and high electronic conductivity.
Furthermore, amorphous composites of metal clusters of one or more of the transition metals and Li2O or LiF at an atomic scale or a nanometer scale also show a high reversible Li-storage behaviour due to the interfacial charging which takes place.
The invention will now be described in more detail with reference to specific embodiments and measurements with reference to the accompanying drawings.
In the drawings there are shown:
FIGS. 2A-F discharge and charge curves of fluorides/Li-cells (with lo=0.2 mA/cm2 if not mentioned),
FIGS. 4A-B Ex situ micro-Raman spectra (
FIGS. 5A-E HRTEM images of TiF3 electrode at different states, namely
Referring first of all to
Present throughout the volume of the electrolyte are also lithium ions 16 shown as circles with a cross in the middle, and anions 18 shown as larger circles with a single line through the middle. When an external circuit is connected to the battery, current flows in the direction opposite to the arrow 20 during discharging and in the direction of the arrow during charging.
It has already been established by others that transition metal oxides, more specifically the oxides Fe, Ni, Co, Cu, show promising performance as anode materials for rechargeable lithium batteries. The reversible Li-storage mechanism is due to the formation and decomposition of Li2O upon the electrochemical insertion/extraction of Li (see references 1 and 2). The key point for the reversibility is related to be the formation of a special microstructure in which metal clusters are dispersed uniformly with Li2O at a nanoscale after electrochemical reaction of metal oxide with Li (again reference is made to the references 1 and 2).
The present applicants had the idea that LiF, which is electrochemically inactive, might be able to show electrochemical activity when it is dispersed with a transition metal at an atomic or nanoscale level. A series of transition metal fluorides (M=Ti, V, Mn, Fe, Co, Ni, Cu) have been investigated and the present description shows the results on TiF3 and VF3 as examples. SnF2 and (CFx)n, where x=1 and n is an integer are also presented for comparison purposes.
The experimental setup was as follows:
An experimental cell in accordance with
The working electrodes 40 and 44 comprised either TiF3A:TiF3:PVDF (9:1 by weight) on Ti foil or TiF3B:TiF3:CB:GP:PVDF (10:0.5:0.5:1 by weight) on Ti foil. Throughout this specification and drawings CB denotes carbon black, GP denotes graphite and PVDF denotes polyvinylene difluoride. the pasting procedures for the electrode film are similar to those reported in H. Li, L. H. Shi, W. Lu, X. J. Huang, L. Q. Chen, J. Electrochem. Soc., 148, A915(2001). It is noted that TiF3 is a commercially available powder with a powder size generally in the range from 300 nm to 5 μm. This size is however not critical. CB is usually available with a particle size up to 40 nm and GP with a particle size in the range from 1 to 10 μm. Again these particle sizes are not critical.
Thus the electrochemical cells tested were 2-electrode cells for electrochemical testing as illustrated in
The electrolyte was:
1M LiPF6, EC-DMC(1:1), Merck, i.e. 1 molar lithium phosphorous fluoride 6, ethylene carbonate-dimethyl carbonate available from Merck, and the investigation was carried out using HRTEM and micro-Raman with procedures similar to those described in the papers by H. Li, X. J. Huang, L. Q. Chen, Electrochem. Soild-State Lett., 1, 241(1998) and H. Li, Y. Mo, N. Pei, X. Xu, X. J. Huang, and L. Q. Chen, J. Phys. Chem. B 104, 8477(2000).
The special electrochemical cell described with reference to
Various examples of electrodes will now be described with reference amongst other things to
The voltage profile of the discharge curves exhibits plateau region at high voltage and slope region at low voltage. The capacity of the plateau region is close to the theoretical capacity of decomposition reaction of fluorides, which is reversible in the cases of TiF3 and VF3. The slope regions for SnF2, TiF3 and VF3 are also reversible, but the former is caused by the Li—Sn alloy reaction (see reference 5), while later (about 250 mAh/g) is related to the insertion of Li into the matrix of LiF/M. Interestingly, (CFx)n also shows partial reversibility. The theoretical capacity and voltage for the decomposition reactions (Plateau region) are as follows:
The results of Raman spectroscopy and XRD investigations are shown in
In
Turning now to
The crystal parameters are as follows:
TiF3: Rhombohedral, d110: 0.388 nm, d110: 0.274 nm, d210: 0.233 nm, d200: 0.223 nm
The ESR results suggest that with insertion of Li ions, the chemical state of Li in the product of the reaction (II) is approaching to metal Li.
From these results, the following conclusions can be drawn:
Here M represents any transition metal.
2. We propose that the extra capacity at the slope region for fluorides is mainly due to the interfacial charging of Li within the matrix of LiF/M, as illustrated in
3. Microstructure of the products in the reaction (I) and (II) is amorphous, which may indicate an atomic-scale dispersion of metal and LiF. This is a key factor for the extraction of Li from LiF.
4. The reversibility of the reaction (IV) is related to metal type and conductive additive (kinetic problem).
This example relates to an electrode in accordance with claim 4. Here the cathode material comprises molybdenum oxide (MoO3) in powder form with an average particle size of 200 nm mixed with a binder in the form of PVDF and deposited on a Ti foil. The mixture ratio was 10:1. The anode was lithium and the electrolyte as used in example 1 (and in the other examples). The reversible capacity was found to be 500 mAh/g.
This example was basically the same as Example 7 but CB and GP were added so that MoO3:CB:GP:PVDF was 10:1:1:1. Here the reversible capacity was found to be 700 mAh/g.
In these examples RuO2 was substituted for MoO3 in the examples 7 and 8. The reversible capacities were found to be 1180 mAh/g and 1200 mAh/g respectively as indicated in
In this example the cathode comprised a LiX—M amorphous nano-composite where:
The mixture was applied as a paste to a Ti foil. The anode was lithium and the same electrolyte was used as in all examples. The reversible capacity obtained was 150 mAh/g in a voltage range of 0-1.2 V.
Here example 11 was repeated but without using CB or GP (LiF:Ti:PVDF=3:1:0.5). LiF and Ti are dispersed at nanoscale. The reversible capacity was 70 mAh/g in a range of 0-1.2 V. Rate performance is shown in
In this example the cathode comprised a LiX-M amorphous nano-composite where:
In this example the cathode comprised a LiX-M amorphous nano-composite where:
Further tests have been carried out using other electrolytes of the various kinds described in the introduction to this application and these tests show that electrode materials described here work well with all these different electrolytes. Furthermore, additional tests have been carried out using different transition metals and different conductive additives in the forms specified in claims 1 and 4 which confirm that the invention works with all the transition metals and conductive additives. Also different halides of the transition metals have been shown to be effective. Moreover, tests carried out substituting ruthenium oxide for molybdenum oxide in Example 9-10 show that this also leads to a very high reversible capacity.
Further background information can be found from the following documents:
Number | Date | Country | Kind |
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102 42 694.5 | Sep 2002 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP03/10138 | 9/11/2003 | WO | 8/19/2005 |