The invention relates to a crystalline nanometric LiFe1-xMxPO4 (LFMP) powder with small particle size and narrow particle size distribution for use as positive electrode material in Li batteries. It also describes a preferred manufacturing method by precipitation at low temperature and atmospheric pressure of the crystalline nanometric powder.
Since the original work of Padhi et al. (JES, 144 (1997), 1188), phospho-olivines LiMPO4 (with M=Fe, Ni, Co, Mn, . . . ) have appeared to be potential candidates to be used as cathode materials for Li batteries. Among all these isostructural compositions, LiFePO4 was the most investigated and its commercialization is now a reality thanks to very high performances in term of reversible capacity, rate properties and cycle life (International Publication Number WO2004/001881 A2).
LiCoPO4 (Amine et al., ESSL, 3, (2000), 178) and LiMnPO4 (Okada et al., J. Power Sources, 97-98 (2001) 430), due to their higher redox potential values oft 4.8 V and 4.1 V vs. Li respect., are of particular interest because of the higher energy density they offer compared to LiFePO4 (3.5V vs. Li, Chen et al., JES, 149 (2002) A1184).
However, it is now well known that these phospho-olivines materials suffer from poor electronic and ionic conductivity (Delacourt et al., JES, 152 (2005) A913) so that the need for optimising the microstructure of these compounds is essential. Striebel et al. (JES, 152, (2005), A664) insisted on the fact that, even if the matrix conductivity has been improved by conductive coating, the battery developer would welcome so-far inexistent compounds having a primary particle size in the 50 to 100 nm range and, overall, attempts should be made to minimise the particle size distribution, in order to yield better power efficiency.
Most promising results on mixed metal phosphates such as LiFe1-xMnxPO4 materials were obtained on C/LiFe0.4Mn0.6PO4 composites, in which C acts as a sintering inhibitor. This approach leads to mixed C/LiFeMnPO4 composites with particles in the 100 to 200 nm range (Mi et al., Mater. Sci. Eng., 129 (2006) 8). Similar results were obtained by Lloris et al. (ESSL, 5 (2002) A234), on pure LiCoPO4 with small particles in the 200 to 300 nm range. No data were published on LiFe1-xCoxPO4 materials so far.
In addition to the small particle size, emphasis must be put on narrowing the particle size distribution in order to ensure a homogeneous current distribution in the electrode and thus achieve better battery performances, in particular high power efficiency and long cycle life. The present invention therefore aims at providing a crystalline LFMP powder with small particle size and narrow particle size distribution.
To this end, a process is disclosed yielding metal phosphate powders offering essential improvements over the materials cited above.
The invented process for the synthesis of crystalline LiFe1-xMxPO4 powder where M is one or both of Co and Mn, and 0<x<1, preferably 0.4<x<0.95, comprises the steps of:
A pH of between 6 and 8 is however preferred to avoid any precipitation of Li3PO4. The additive is preferably a dipolar aprotic compound without chelating or complexation propensity. The heating temperature of the water-based mixture of at least 60° C. is preferred.
The production of the crystalline LiFe1-xMxPO4 powder or the thermal post-treatment can advantageously be performed in the presence of at least one further component, in particular a carbon containing or electron conducting substance, or the precursor of an electron conducting substance.
It is useful to introduce at least part of the Li(I) is as LiOH. Similarly, at least part of the P(V) can be introduced as H3PO4. The pH of the water-based mixture can be obtained by adjusting the ratio of LiOH to H3PO4.
It is advisable to use a water-based mixture with an atmospheric boiling point of between 100 and 150° C., and preferably between 100 and 120° C. Dimethylsulfoxide (DMSO) is preferably used as the dipolar aprotic additive. The water-based mixture advantageously contains between 5 and 50% mol, and preferably between 10 and 30% mol, of DMSO. A lower DMSO concentrations result in a coarser particle size distribution; higher concentrations limit the availability of water, forcing to increase the volume of the apparatus.
The step of post treatment of the LiFe1-xMxPO4 is advantageously performed at a temperature of up to 675° C., and preferably of at least 300° C. The lower limit is chosen in order to enhance the crystallinity of the precipitated LiFe1-xMxPO4; the upper limit is chosen so as to avoid the decomposition of the LiFe1-xMxPO4 into manganese phosphides.
The electron conducting substance can be carbon, in particular conductive carbon or carbon fibres. Alternatively, a precursor of an electron conducting substance can be used, in particular a polymer or sugar-type macromolecule.
The invention also pertains to a crystalline LiFe1-xMnxPO4 powder with 0<x<1, preferably 0.4<x<0.95, for use as electrode material in a battery, having a particle size distribution with an average particle size d50 of less than 100 nm, and preferably of more than 30 nm. The maximum particle size is preferably less than or equal to 500 nm. The particle size distribution is preferably mono-modal and the ratio (d90−d10)/d50 is advantageously less than 1.5, preferably less than 1.3.
Another embodiment of this invention concerns a composite powder containing the above-defined crystalline LiMnPO4 powder, and up to 10% wt of conductive additive. A further embodiment concerns the electrode mix that can be prepared using this composite powder. Conductive carbons, carbon fibres, amorphous carbons resulting from decomposition of organic carbon containing substances, electron conducting polymers, metallic powders, and metallic fibres are particularly well suited as conductive additives.
Another embodyment of this invention concerns the use of the composite powder for the manufacture of a lithium insertion-type electrode, by mixing said powder with a conductive carbon-bearing additive.
The invention also pertains to a crystalline LiFe1-xCoxPO4 powder with 0<x<1, preferably 0.4<x<0.95, for use as electrode material in a battery, having a particle size distribution with an average particle size d50 of less than 300 nm, and preferably of more than 30 nm. The maximum particle size is preferably less than or equal to 900 nm. The particle size distribution is preferably mono-modal and the ratio (d90−d10)/d50 is advantageously less than 1.5, preferably less than 1.1.
Another embodiment of this invention concerns a composite powder containing the above-defined crystalline LiFe1-xCoxPO4 powder, and up to 10% wt of conductive additive. A further embodiment concerns the electrode mix that can be prepared using this composite powder. Conductive carbons, carbon fibres, amorphous carbons resulting from decomposition of organic carbon containing substances, electron conducting polymers, metallic powders, and metallic fibres are particularly well suited as conductive additives.
Another embodyment of this invention concerns the use of the composite powder for the manufacture of a lithium insertion-type electrode, by mixing said powder with a conductive carbon-bearing additive.
Compared to prior art, this product lists all the advantages needed for being considered as potential cathode material in lithium battery:
The atmospheric boiling point of the water-based mixture is advisably between 100 and 150° C., preferably between 100 and 120° C. Use is made of a water-miscible additive as a co-solvent that will increase the precipitate nucleation kinetics thus reducing the size of the LiMnPO4 nanometric particles. In addition to be miscible with water, useful co-solvents should be aprotic, i.e. show only a minor or complete absence of dissociation accompanied by release of hydrogen ions. Co-solvents showing complexation or chelating properties such as ethylene glycol do not appear suitable as they will reduce the kinetics of precipitation of LiMnPO4 and thus lead to larger particle sizes. Suitable dipolar aprotic solvents are dioxane, tetrahydrofuran, N-(C1-C18-alkyl)pyrrolidone, ethylene glycol dimethyl ether, C1-C4-alkylesters of aliphatic C1-C6-carboxylic acids, C1-C6-dialkyl ethers, N,N-di-(C1-C4alkyl)amides of aliphatic C1-C1-carboxylic acids, sulfolane, 1,3-di-(C1-C8-alkyl)-2-imidazolidinone, N-(C1-C8-alkyl)caprolactam, N,N,N′, N′-tetra-(C1-C8-alkyl)urea, 1,3-di-(C1-C8-alkyl)-3,4,5,6-tetrahydro-2(1H)-pyrimidone, N,N,N′,N′-tetra-(C1-C8-alkyl)sulfamide, 4-formylmorpholine, 1-formylpiperidine or 1-formylpyrrolidine, N-(C1-C18-alkyl)pyrrolidone, N-methylpyrrolidone (NMP), N-octylpyrrolidone, N-dodecylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide or hexamethylphosphoramide. Other alternatives such as tetraalkyl ureas are also possible. Mixtures of the abovementioned dipolar aprotic solvents may also be used. In a preferred embodiment, dimethylsulfoxide (DMSO) is used as solvent.
The Figures illustrating the invention are summarized as follows.
The invention is further illustrated in the following examples.
In a first step, DMSO is added to an equimolar solution of 0.05 M Mn(II) in MnNO3.4H2O, 0.05 M Fe(II) in FeSO4.7H2O and 0.1 M P(V) in H3PO4, dissolved in H2O while stirring. The amount of DMSO is adjusted in order to reach a global composition of 50% vol water and 50% vol DMSO corresponding to respectively about 80% mol and 20% mol.
In a second step, an aqueous solution of 0.3 M LiOH.H2O is added to the solution at 25° C.; the pH hereby increases to a value between 6.5 and 7.5. The final Li:Fe:Mn:P ratio is close to 3:0.5:0.5:1.
In a third step, the temperature of the solution is increased up to the solvent boiling point, which is 108 to 110° C. After 18 h, the obtained precipitate is filtered and washed thoroughly with water. The pure crystalline LiFe0.5Mn0.5PO4 obtained is shown in
The refined cell parameters are a=10.390 Å, b=6.043 Å; c=4.721 Å, with a cell volume of 296.4 Å3. This is in good agreement with Vegard's law specifying that, in case of solid solution, the cell volume of mixed product should be in-between that of end products (291 Å3 for pure LiFePO4, 302 Å3 for pure LiMnPO4).
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In a first step, DMSO is added to an equimolar solution of 0.05 M Mn(II) in MnSO4.H2O, 0.05 M Co(II) in CoNO3.6H2O and 0.1 M P(V) in H3PO4, dissolved in H2O while stirring. The amount of DMSO is adjusted in order to reach a global composition of 50% vol. water and 50% vol. DMSO.
In a second step, an aqueous solution of 0.3 M LiOH.H2O is added to the solution at 25° C.; the pH hereby increases to a value between 6.5 and 7.5. The, the final Li:Fe:Co:P ratio is close to 3:0.5:0.5:1.
In a third step, the temperature of the solution is increased up to the solvent boiling point, which is 108 to 110° C. After 18 h, the obtained precipitate is filtered and washed thoroughly with water. The pure crystalline LiFe0.5Co0.5PO4 obtained is shown in
The refined cell parameters are a=10.292 Å, b=5.947 Å; c=4.712 Å with a cell volume of 288.4 Å3. This is again in good agreement with Vegard's law specifying that, in case of solid solution, the cell volume of mixed product should be in-between that of end products (291 Å3 for pure LiFePO4, 284 Å3 for pure LiCoPO4).
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Number | Date | Country | Kind |
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06292048 | Dec 2006 | EP | regional |
This application is a National Stage application of International Application No. PCT/EP2007/009969, filed Nov. 19, 2007, which claims priority to European Patent Application No. 06292048.3, filed Dec. 22, 2006, and U.S. Provisional Patent Application No. 60/881,509, filed Jan. 22, 2007, the entire contents of which are hereby incorporated by reference.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2007/009969 | 11/19/2007 | WO | 00 | 9/30/2009 |
Publishing Document | Publishing Date | Country | Kind |
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WO2008/077448 | 7/3/2008 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
5910382 | Goodenough et al. | Jun 1999 | A |
6749967 | Li et al. | Jun 2004 | B2 |
7390472 | Singhal et al. | Jun 2008 | B1 |
7771628 | Barker et al. | Aug 2010 | B2 |
20030215718 | Huang et al. | Nov 2003 | A1 |
20040175614 | Wurm et al. | Sep 2004 | A1 |
20060035148 | Balaya et al. | Feb 2006 | A1 |
20060035150 | Audemer et al. | Feb 2006 | A1 |
20070031732 | Chiang et al. | Feb 2007 | A1 |
20080241690 | Delacourt et al. | Oct 2008 | A1 |
20100086852 | Gibot et al. | Apr 2010 | A1 |
Number | Date | Country |
---|---|---|
2004-079276 | Mar 2004 | JP |
2004079276 | Mar 2004 | JP |
2004259470 | Sep 2004 | JP |
2006025842 | Mar 2006 | KR |
WO 02083555 | Oct 2002 | WO |
WO 02099913 | Dec 2002 | WO |
WO 04001881 | Dec 2003 | WO |
WO 2004056702 | Jul 2004 | WO |
WO 2005051840 | Jun 2005 | WO |
WO 2006105848 | Oct 2006 | WO |
WO 2007000251 | Jan 2007 | WO |
WO 2008018633 | Feb 2008 | WO |
WO 2008077447 | Jul 2008 | WO |
WO 2008077448 | Jul 2008 | WO |
WO 2008113570 | Sep 2008 | WO |
Number | Date | Country | |
---|---|---|---|
20100084615 A1 | Apr 2010 | US |
Number | Date | Country | |
---|---|---|---|
60881509 | Jan 2007 | US |