Production of a spinel material
09834854 · 2017-12-05
Assignee
Inventors
Cpc classification
H01M4/525
ELECTRICITY
C01P2002/74
CHEMISTRY; METALLURGY
C01P2002/77
CHEMISTRY; METALLURGY
H01M4/505
ELECTRICITY
Y02E60/10
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
C01G53/54
CHEMISTRY; METALLURGY
C01P2002/72
CHEMISTRY; METALLURGY
International classification
H01M4/525
ELECTRICITY
Abstract
A process for producing a lithium-manganese-nickel oxide spinel material includes maintaining a solution comprising a dissolved lithium compound, a dissolved manganese compound, a dissolved nickel compound, a hydroxycarboxylic acid, a polyhydroxy alcohol, and, optionally, an additional metallic compound, at an elevated temperature T.sub.1, where T.sub.1 is below the boiling point of the solution, until the solution gels. The gel is maintained at an elevated temperature until it ignites and burns to form a Li—Mn—Ni—O powder. The Li—Mn—Ni—O powder is calcined to burn off carbon and/or other impurities present in the powder. The resultant calcined powder is optionally subjected 1 to microwave treatment, to obtain a treated powder, which is annealed to crystallize the powder. The resultant annealed material is optionally subjected to microwave treatment. At least one of the microwave treatments is carried out. The lithium-manganese-nickel oxide spinel material is thereby obtained.
Claims
1. A process for producing a lithium-manganese-nickel oxide spinel material, which process comprises maintaining a solution comprising a dissolved lithium compound, a dissolved manganese compound, a dissolved nickel compound, a hydroxycarboxylic acid, a polyhydroxy alcohol, and, optionally, an additional metallic compound, at an elevated temperature T.sub.1, where T.sub.1 is below the boiling point of the solution, until the solution gels; maintaining the gel at an elevated temperature until it ignites and burns to form a Li—Mn—Ni—O powder; calcining the Li—Mn—Ni—O powder to burn off carbon and/or other impurities present in the powder, thereby obtaining a calcined powder; subjecting the calcined powder to microwave treatment, to obtain a treated powder; and annealing the treated powder to crystallize the powder, thereby obtaining an annealed lithium-manganese-nickel-oxide spinel material.
2. The process according to claim 1, wherein the solution includes water as a solvent for the lithium compound, the manganese compound, and the nickel compound, which are thus water soluble salts thereof, with 90° C.≦T.sub.1<100° C.
3. The process according to claim 2, wherein T.sub.1 is about 90° C.
4. The process according to claim 1, wherein the elevated temperature at which the gel is maintained is T.sub.2, where 90° C.≦T.sub.2<100° C.
5. The process according to claim 4, wherein T.sub.2 is about 90° C.
6. The process according to claim 1, wherein the calcination of the Li—Mn—Ni—O powder is effected at a temperature T.sub.3, where 400° C.≦T.sub.3<600°C.
7. The process according to claim 6, wherein T.sub.3 is about 500° C.
8. The process according to claim 1, wherein the annealing of the treated powder is effected at a temperature T.sub.4, where 700° C.≦T.sub.4 ≦900° C.
9. The process according to claim 8, wherein 700° C.≦T.sub.4 ≦800° C.
10. The process according to claim 1, wherein the lithium-manganese-nickel oxide spinel material is undoped, and is LiMn.sub.1.5Ni.sub.0.5O.sub.4.
11. The process according to claim 1, wherein the lithium-manganese-nickel oxide spinel material is doped.
12. The process according to claim 11, wherein the lithium-manganese-nickel oxide spinel material is ordered so that it is not oxygen deficient.
13. The process according to claim 1, which includes using the additional metallic compound to improve stability of the spinel material, with the additional metallic compound being a compound of aluminium or zirconium.
14. The process according to claim 1, wherein the hydroxycarboxylic acid is citric acid.
15. The process according to claim 14, wherein the polyhydroxy alcohol is ethylene glycol.
16. The process according to claim 15, wherein the citric acid and the ethylene glycol are present in the solution in a molar ratio of citric acid to ethylene glycol of about 1:4.
17. The process according to claim 1, wherein the microwave treatment comprises subjecting the calcined powder to microwaves at about 60° C. for between 10 and 20 minutes.
18. The process according to claim 1, further comprising subjecting the annealed lithium-manganese-nickel-oxide spinel material to a second microwave treatment.
19. The process according to claim 18, wherein the second microwave treatment comprises subjecting the annealed lithium-manganese-nickel-oxide spinel material to microwaves at about 60° C. for between 10 and 20 minutes.
20. A process for producing a lithium-manganese-nickel oxide spinel material, which process comprises maintaining a solution comprising a dissolved lithium compound, a dissolved manganese compound, a dissolved nickel compound, a hydroxycarboxylic acid, a polyhydroxy alcohol, and, optionally, an additional metallic compound, at an elevated temperature T.sub.1, where T.sub.1 is below the boiling point of the solution, until the solution gels; maintaining the gel at an elevated temperature until it ignites and burns to form a Li—Mn—Ni—O powder; calcining the Li—Mn—Ni—O powder to burn off carbon and/or other impurities present in the powder, thereby obtaining a calcined powder; subjecting the calcined powder to microwave treatment at a maximum temperature of 60° C. , to obtain a treated powder; and annealing the treated powder to crystallize the powder, thereby obtaining an annealed lithium-manganese-nickel-oxide spinel material.
Description
(1) The invention will now be described in more detail with reference to the following non-limiting example and accompanying drawings. In the drawings
(2)
(3)
(4)
(5)
(6)
(7)
(8)
EXAMPLE
(9) LiMn.sub.1.5Ni.sub.0.5O.sub.4 (LMN) was prepared by a one-step powder-forming, Pechini modified method involving the use of citric acid (CA), ethylene glycol (EG) and nitrate salts. The reducing agent, CA (dissolved in deionised water) and EG was mixed in the ratio 1:4 (CA:EG) and heated at 90° C. while constantly stirred for 30 min. Stoichiometric amounts of LiNO.sub.3, Ni(NO.sub.3).sub.2.6H.sub.2O and Mn(NO.sub.3).sub.2.4H.sub.2O were dissolved in deionised water and introduced drop-wise to the CA/EG solution. After heating the resultant solution to, and maintaining it at, 90° C. with constant stirring, the viscosity of the solution increased constantly due to evaporation of the water; the viscous solution subsequently dehydrated into a gel. The gel was kept at a temperature of 90° C. until the gel spontaneously burnt (typically about 30 minutes after the salt-containing solution was added to the reducing agent) to form the desired powder. The powder was pre-heated, i.e. calcined, at 500° C. for 6 h to get rid of carbonaneous materials present on the powder from the burning, and then annealed at 700° C. or 800° C. for 8 h (herein referred to as LMN-700 or LMN-800, respectively). To study the impact of microwave irradiation, two batches of the pre-heated powder at 500° C. were subjected to microwave irradiation (using the Anton Paar Multiwave 3000 system, λ=0.12236 m) at 600 W for 15 min, where the temperature of the samples reached a maximum of 60° C. (measured with an infrared thermometer, which was approximately 5 cm away from the bottom of the vessel containing the powders), and then annealed at 700° C. or 800° C. for 8 h (herein referred to as LMN-700-mic or LMN-800-mic, respectively).
(10) The structural characterization was done by XRD using a Bruker AXS D8 ADVANCE X-ray Diffractometer with Ni-filtered Cu K.sub.α radiation (λ=1.5406 Å) for the LMN-700/LMN-700-mic and a PANalytical X'pert Pro Powder Diffractometer with Fe-filtered Co K.sub.α radiation (λ=1.7890 Å) for the LMN-800/LMN-800-mic. The scanning speed was 0.02° per step with a dwell time of 5 s for all samples. The LMN-700/LMN-700-mic and LMN-800/LMN-800-mic powders were mounted in a PHI 5400 ESCA and PHI 5000 Versaprobe -Scanning ESCA Microprobe vacuum chambers with base pressures 1×10.sup.−8 Torr. XPS was performed for LMN-700/LMN-700-mic and LMN-800/LMN-800-mic using a non-monochromatic aluminium (Al) K.sub.α source (1486.6 eV) and an Al monochromatic K.sub.α source (1486.6 eV), respectively. The XPS data analysis was performed with the XPS Peak 4.1 program and a Shirley function was used to subtract the background.
(11) Electrochemical measurements were performed in a two-electrode coin cell (LIR-2032) assembled with the LMN materials as the positive electrode and lithium metal foil as the negative electrode using a MACCOR series 4000 tester. The cathodes were prepared by coating the slurry of a mixture composed of 80% active material, 10% acetylene black, and 10% polyvinylidene fluoride onto cleaned and polished aluminium foil. Subsequently, the materials were dried at 90° C. under vacuum (˜10.sup.−1 Torr) for 24 h. The cells were assembled in an argon-filled MBraun glovebox (O.sub.2, H.sub.2O<0.5 ppm). The electrolyte was 1M LiPF.sub.6 in a mixture of 1:1 (v/v) EC:DMC. A polypropylene film (Celgard 2300, Celgard LLC, Charlotte, N.C., USA) was used as the separator.
(12) SEM Analysis (Morphological Analysis)
(13) Mesoporous structures were expected as already observed in the literature for LMN. As can be seen from
(14) XRD Analysis (Structural Analysis)
(15)
(16) The powder XRD patterns (
(17) XPS Analysis (Oxidation States Analysis)
(18) To determine the actual amounts of the Mn.sup.3+ and Mn.sup.4+ in the spinel, XPS experiments were performed for the powdered spinel samples.
(19) TABLE-US-00001 TABLE 1 Mn 2p.sub.3/2 peak positions and cation distribution Binding energy position (eV) Cation distribution Sample Mn.sup.4+ Mn.sup.3+ Mn.sup.4+ Mn.sup.3+ Mn.sup.3+/Mn.sup.4+ LMN-700 643.2 642.1 31.5% 68.5% 2.17 LMN-700-mic 643.4 642.2 23.4% 76.6% 3.27 LMN-800 643.4 642.1 27.9% 72.1% 2.58 LMN-800-mic 643.3 641.9 37.5% 62.5% 1.67
Discharge Capacities
(20)
(21) Capacity Retention (Cyclability) and Rate Capability
(22) The cycle stability of the spinel samples at 50 repetitive cycles was explored.
(23) As indicated by the
(24) For high power applications, good rate capability is of utmost importance for any cathode materials for lithium ion battery. All the samples were charged at 14 mA/g (0.1 C) and discharged at 140 mA/g (1 C) and the 800° C. samples showed the best performance (
(25) The electrochemical performance of LiMn.sub.1.5Ni.sub.0.5O.sub.4 as a lithium ion battery cathode material is intricately linked to the (i) presence of Mn.sup.3+ ions, (ii) doping/substitution, (iii) degree of disorder, and (iv) impurities, which explains why it still remains a huge challenge to correlate synthesis, structure and performance of this cathode material. It is common knowledge that the Mn.sup.3+ ion is electrochemically active, usually identified by the presence of a small plateau at around 4V; however, a portion of the Mn.sup.3+ ions may also form Mn.sup.2+ through the disproportion reaction; Mn.sup.2+ dissolves into the electrolyte at elevated temperatures, causing significant capacity loss during cycling (J. Xiao, X. Chen, P. V. Sushko, M. L. Sushko, L. Kovarik, J. Feng, Z. Deng, J. Zheng, G. L. Graff, Z. Nie, D. Choi, J. Liu, J.- G. Zhang, M. S. Whittingham, Adv. Mater. 24 (2012) 2109-2116). To enhance the cyclability and eliminate the impurities in the LiMn.sub.1.5Ni.sub.0.5O.sub.4, a commonly adopted approach hitherto has been to partially substitute Ni and/or Mn with metallic elements, such as Ti, Fe, Cr, Ru or Mg. A disordered or oxygen-deficient spinel (i.e. LiMn.sub.1.5Ni.sub.0.5O.sub.4-δ) is usually accompanied by an impurity (Li.sub.yNi.sub.1-yO) that appears as a secondary phase in the products, which lowers the obtainable capacity. However, the cycling performance of the disordered spinel is better than the ordered spinel as the former gives a significantly higher Li.sup.+ diffusion coefficient than the latter. In ordered P4.sub.332 phase, Mn.sup.4+ and Ni.sup.2+ ions are ordered on octahedral sites in a 3:1 ratio as opposed to random distribution in disordered Fd.sub.3m phase.
(26) The Xiao et al reference referred to above, indicates ‘careful control of the amount of Mn.sup.3 ions and, thus, the disordered phase, is the key for synthesis of high performance spinel and provides valuable clues for understanding the structure-property relationships in energy materials’.
(27) The electrochemical performance of any chemical material is strongly dependent on the synthesis strategy. It is evident from what is set out above that the preferred synthesis strategy for the high-voltage LiMn.sub.1.5Ni.sub.0.5O.sub.4 spinel should be able to (i) control the amount of the Mn.sup.3+ in the final lattice structure, and hence the site disorder, (ii) limit the amount of the Li.sub.yNi.sub.1-yO impurity, and (iii) maintain its high voltage (4.8-5V) and achieve capacity close or better than the theoretical value of ˜140 mAh/g.sup.−1.
(28) The inventors thus surprisingly found that by using a modified Pechini synthesis strategy coupled with microwave irradiation, a LiMn.sub.1.5Ni.sub.0.5O.sub.4 spinel cathode material with desired properties could be obtained. For example, the inventors proved, for the first time, that it is possible to control the Mn.sup.3+ content and site disorder by a simple microwave treatment. The inventors thus found that they could achieve the same or better results to those achievable by known processes, and using shorter processing times, by using low temperature annealing coupled with short duration 20 minutes) microwave irradiation.
(29) Simply stated, the microwave-assisted strategy introduced by the inventors for the preparation and enhancing the electrochemical performance of LiMn.sub.1.5Ni.sub.0.5O.sub.4 spinel materials promises to avoid many of the disadvantages associated with conventional procedures of making this spinel cathode material.