NZ310242A - Process for making a lithiated lithium manganese oxide spinel by contacting a lithium magnesium oxide spinel and a lithium carboxylate compound - Google Patents
Process for making a lithiated lithium manganese oxide spinel by contacting a lithium magnesium oxide spinel and a lithium carboxylate compoundInfo
- Publication number
- NZ310242A NZ310242A NZ310242A NZ31024296A NZ310242A NZ 310242 A NZ310242 A NZ 310242A NZ 310242 A NZ310242 A NZ 310242A NZ 31024296 A NZ31024296 A NZ 31024296A NZ 310242 A NZ310242 A NZ 310242A
- Authority
- NZ
- New Zealand
- Prior art keywords
- lithium
- spinel
- hours
- lithiated
- reaction
- Prior art date
Links
- 229910052596 spinel Inorganic materials 0.000 title claims abstract description 93
- 239000011029 spinel Substances 0.000 title claims abstract description 93
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 30
- -1 lithium carboxylate compound Chemical class 0.000 title claims abstract description 17
- 229910002102 lithium manganese oxide Inorganic materials 0.000 title abstract description 17
- VLXXBCXTUVRROQ-UHFFFAOYSA-N lithium;oxido-oxo-(oxomanganiooxy)manganese Chemical compound [Li+].[O-][Mn](=O)O[Mn]=O VLXXBCXTUVRROQ-UHFFFAOYSA-N 0.000 title abstract description 17
- ORUCDOXAKFCOJF-UHFFFAOYSA-N [O-2].[Mg+2].[Li+] Chemical compound [O-2].[Mg+2].[Li+] ORUCDOXAKFCOJF-UHFFFAOYSA-N 0.000 title 1
- 239000000843 powder Substances 0.000 claims description 38
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 238000006243 chemical reaction Methods 0.000 claims description 27
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 claims description 25
- 239000002002 slurry Substances 0.000 claims description 25
- 239000000376 reactant Substances 0.000 claims description 23
- 229910052786 argon Inorganic materials 0.000 claims description 19
- 238000000634 powder X-ray diffraction Methods 0.000 claims description 16
- 229910014549 LiMn204 Inorganic materials 0.000 claims description 14
- 150000001875 compounds Chemical class 0.000 claims description 13
- 229940071264 lithium citrate Drugs 0.000 claims description 11
- WJSIUCDMWSDDCE-UHFFFAOYSA-K lithium citrate (anhydrous) Chemical compound [Li+].[Li+].[Li+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O WJSIUCDMWSDDCE-UHFFFAOYSA-K 0.000 claims description 11
- 239000011572 manganese Substances 0.000 claims description 10
- 239000000725 suspension Substances 0.000 claims description 9
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 229910052748 manganese Inorganic materials 0.000 claims description 8
- 238000004458 analytical method Methods 0.000 claims description 7
- GKQWYZBANWAFMQ-UHFFFAOYSA-M lithium;2-hydroxypropanoate Chemical compound [Li+].CC(O)C([O-])=O GKQWYZBANWAFMQ-UHFFFAOYSA-M 0.000 claims description 7
- 150000007942 carboxylates Chemical class 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000012300 argon atmosphere Substances 0.000 claims description 3
- 239000012298 atmosphere Substances 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- FBDMJGHBCPNRGF-UHFFFAOYSA-M [OH-].[Li+].[O-2].[Mn+2] Chemical compound [OH-].[Li+].[O-2].[Mn+2] FBDMJGHBCPNRGF-UHFFFAOYSA-M 0.000 claims 4
- 229910013594 LiOAc Inorganic materials 0.000 claims 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 abstract description 13
- 229910002097 Lithium manganese(III,IV) oxide Inorganic materials 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 239000000243 solution Substances 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910002804 graphite Inorganic materials 0.000 description 5
- 239000010439 graphite Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 229910001416 lithium ion Inorganic materials 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 230000004580 weight loss Effects 0.000 description 3
- 229910010229 Li2Mn204 Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000002687 intercalation Effects 0.000 description 2
- 238000009830 intercalation Methods 0.000 description 2
- HSZCZNFXUDYRKD-UHFFFAOYSA-M lithium iodide Chemical compound [Li+].[I-] HSZCZNFXUDYRKD-UHFFFAOYSA-M 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 239000011872 intimate mixture Substances 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 229910052743 krypton Inorganic materials 0.000 description 1
- 229910003002 lithium salt Inorganic materials 0.000 description 1
- 159000000002 lithium salts Chemical class 0.000 description 1
- XKPJKVVZOOEMPK-UHFFFAOYSA-M lithium;formate Chemical compound [Li+].[O-]C=O XKPJKVVZOOEMPK-UHFFFAOYSA-M 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 229910052754 neon Inorganic materials 0.000 description 1
- 229910052756 noble gas Inorganic materials 0.000 description 1
- 150000002835 noble gases Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 125000005010 perfluoroalkyl group Chemical group 0.000 description 1
- 229910052704 radon Inorganic materials 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910052724 xenon Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G45/00—Compounds of manganese
- C01G45/12—Complex oxides containing manganese and at least one other metal element
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G45/00—Compounds of manganese
- C01G45/12—Complex oxides containing manganese and at least one other metal element
- C01G45/1221—Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof
- C01G45/1242—Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof of the type (Mn2O4)-, e.g. LiMn2O4 or Li(MxMn2-x)O4
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G45/00—Compounds of manganese
- C01G45/12—Complex oxides containing manganese and at least one other metal element
- C01G45/1221—Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof
- C01G45/125—Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof of the type (MnO3)n-, e.g. CaMnO3
- C01G45/1257—Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof of the type (MnO3)n-, e.g. CaMnO3 containing lithium, e.g. Li2MnO3 or Li2(MxMn1-x)O3
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/30—Three-dimensional structures
- C01P2002/32—Three-dimensional structures spinel-type (AB2O4)
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Disclosed is a process for making a lithiated lithium manganese oxide spinel of the formula Li(1+x)Mn204 comprising contacting a lithium manganese oxide spinel of the formula LiMn2O4 with a lithium carboxylate compound, at a temperature and for a time sufficient to decompose the carboxylate compound and free the lithium to form said lithiated spinel.
Description
<div class="application article clearfix" id="description">
<p class="printTableText" lang="en">New Zealand Paient Spedficaiion for Paient Number 310242 <br><br>
New Zealand No. 310242 International No. PCT/US96/09461 <br><br>
TO BE ENTERED AFTER ACCEPTANCE AND PUBLICATION <br><br>
Priority dates: 07.06.1995; <br><br>
Complete Specification Filed: 05.06.1996 <br><br>
Classification:^) C01G45/12 <br><br>
Publication date: 25 November 1998 <br><br>
Journal No.: 1434 <br><br>
Title of Invention: <br><br>
An improved process for making a lithiated lithium manganese oxide spinel <br><br>
Name, address and nationality of applicant(s) as in international application form: <br><br>
DURACELL INC., Berkshire Corporate Park, Bethel, Connecticut 06801, United States of America <br><br>
NEW 2EALAND PATENTS ACT 1953 <br><br>
COMPLETE SPECIFICATION <br><br>
310242 <br><br>
PCT/US96/09461 <br><br>
AN IMPROVED PROCESS FOR MAKTMa A LITHIATED LITHIUM MANGANESE OXIDE SPINEL <br><br>
The present invention relates to an improved process for making a lithiated spinel compound. In particular, the invention relates to a process for lithiating a lithium manganese oxide spinel to form a spinel featuring excess lithium, which ' is useful as an electrochemically active component in a secondary electrochemical cell. <br><br>
Lithium secondary, electrochemical cells, or rechargeable cells, typically include a Li-bearing intercalation compound as the positive electrode and a carbon, typically graphite, negative electrode, separated by a non-aqueous lithium-ion electrolyte. A lithium manganese oxide spinel of the general formula LiMnj04 commonly has been employed as the electrochemically active cathode component. Studies of lithium intercalation into graphite have shown, however, that when the lithium manganese oxide spinel is used in a lithium-ion rechargeable cell in which the anode or negative electrode is graphite, there is a marked, detrimental irreversible loss in capacity during the first recharging cycle. The initial approach to overcome this problem was simply to use a larger mass of positive electrode [ (1+x) LiMn20J to compensate for the loss of lithium on the graphite anode during the first cycle. However, increasing the mass of the cathode is not an effective remedy when taking performance efficiency into consideration. In order to offset the lithium loss without, undesirably, seriously impacting massic or volumetric performance characteristics of the cell, lithiated lithium manganese oxide spinel structures have been developed which feature excess lithium (Li,ltx)Mn204) . This excess lithium in the spinel compound <br><br>
1 <br><br>
WO 96/40590 <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
is available to compensate for the initial loss of lithium ( <br><br>
associated with the negative electrode, while reserving an amount of lithium needed to balance the reversible capacity of the graphite and maintain a useful energy level in the cell. <br><br>
While such lithiated lithium manganese oxide spinel compounds have proven to be a useful and effective cathode material in secondary or rechargeable electrochemical cells, presently known methods for producing the Li(1+x)Mn204 spinel are expensive and difficult to scale up from laboratory size to commercial volume. One such method of production, for example, includes subjecting LiMn204 to a reducing reaction with a heated solution of lithium iodide (Lil) in acetonitrile; another involves a reduction of the lithium manganese oxide spinel with a solution of n-butyl lithiate (n-BuLi) in hexane. Both of these lithium-containing reactants are prohibitively expensive, the production processes involve organic solvents, and, in addition, the n-BuLi features hazardous, pyrophoric properties. Accordingly, there is a need for a viable method for commercial production of the lithiated lithium manganese oxide spinel. <br><br>
It now has been discovered that a lithiated lithium manganese oxide spinel of the formula Li(1+x,Mn204 can economically be made by a simple method which comprises contacting a lithium manganese oxide spinel of the formula LiMn204 with a lithium carboxylate compound, at a temperature and for a time sufficient to decompose the carboxylate compound and free the lithium to form said lithiated, <br><br>
Lia<.x)Mn204 spinel. This lithiated spinel compound has been found to be particularly useful as the positive electrode of a lithium-ion secondary electrochemical cell. <br><br>
2 <br><br>
fr . <br><br>
. ^WO 96/40590' ,.vPCT/yS96/Q946r <br><br>
; The object of the present invention is to provide a process which produces a lithiated lithium manganese oxide spinel of the formula Li(x+x|Mn,04i, wherein 0<x<l; preferably, the value of x ranges from about .05 to about 1.0; most preferably, x ranges from about .05 to about .3, or at least provides the public with a useful choice. <br><br>
The process is carried at a reaction temperature sufficient to decompose the lithium carboxylate reactant and form the lithiated spinel compound, but, below, about . 350°C, to avoid decomposition of the spinel' compound. Above about 300°C the spinel compound begins to decompose into non-spinel decomposition products such as "Lin^MnO, and MnO,, which are not. useful as cathode components in a lithium secondary electrochemical cell. The reaction temperature generally ranges from about 150°C to about 300°C; preferably, the reaction temperature ranges from about 230°C to about 250°C. <br><br>
Reaction time is dependent upon choice of reactants and reaction temperature. In general, reaction time ranges from about 10 minutes to about 15 hours; preferably about 2 to about 8 hour reaction times are employed, since such times have been found to provide favorable results. <br><br>
Preferably, the synthesis is conducted in an inert atmosphere: to avoid oxidation' reactions resulting in the formation of by products undesirable for electrochemical cathode utility, such "as LijCBj and/or LiaMn03. Suitable inert atmospheres include the noble gases (He, Ne, Ar, Kr, Xe, and Rn), vacuum, and combinations thereof, and the like. An argon atmosphere is preferred. <br><br>
'•N <br><br>
The lithium carboxylate reactant employed in the present process is any lithium salt of mono and -polycarboxylic acids, which features a decomposition temperature below about 300°C, and <br><br>
09 OCT 1998 RECEIVED'. <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
which is effective to lithiate a LiMn204 spinel when heated in (" <br><br>
contact with said spinel at a temperature below about 300°C. <br><br>
Examples of suitable lithium carboxylates useful in the present process include lithium acetate, lithium citrate, lithium formate, lithium lactate, other lithium carboxylates in which the carboxylate group is attached to a group that is election-withdrawing relative to methyl (such as hydrogen, <br><br>
perfluoroalkyl, CF3S02CH2, and (CF3S02)2N ), and the like. Lithium acetate is particularly preferred as the lithium carboxylate reactant. <br><br>
The process of the present invention may be practiced using various techniques. In one embodiment, particulate LiMn204 spinel first is mixed with a solution, preferably an aqueous solution, of lithium carboxylate to form a paste. Then, the paste is dried to remove the solvent and the so-formed intimate admixture of spinel and carboxylate is heated to a temperature and for a time sufficient to decompose the carboxylate and initiate reaction to form the Li(ltx)Mn204 spinel. <br><br>
In another alternative embodiment of the process, the particulate LiMn204 spinel and the lithium carboxylate salt are dry-mixed to form an intimate mixture. The dry admixture then is heat treated to lithiate the spinel to form the desired Liu+x)Mn204 product. Any suitable dry mixing technique may be used to form the reactant mixture; such techniques include drum mixers, ball mixers, rod mixers, and the like. <br><br>
In a preferred process, lithium acetate; as the lithium carboxylate reactant, is dissolved in water, and lithium manganese oxide spinel is added to the solution to form a paste. The Li0Ac/LiMn204 paste then is air dried at a temperature of <br><br>
4 <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
about 50°C to about 150°C, preferably about 100°C. The dried admixture next is reacted by heating it in an argon atmosphere to a temperature from about 230°C to about 250°C for a period of about 2 to about 8 hours. <br><br>
The following examples are provided to further illustrate the invention. <br><br>
Example 1 <br><br>
Lithiated spinel of the formula Li^MnjO* is prepared by dissolving 1.695 grams of lithium acetate (LiOAc) in about 30ml of deionized (DI) water. A stoichiometric amount of particulate lithium manganese oxide LiMn30, spinel, 30 grams, is added to the LiOAc solution and the resulting slurry is stirred to keep the spinel in suspension and to ensure homogeneity between the spinel and LiOAc reactants, while the slurry is heated at 80-90°C for about 3 hours to remove excess water and convert the slurry into a paste. The paste then is vacuum dried at 80°C. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1.5 hours, and is held at that temperature for 2 hours to form a bluish black powder product. The powder is cooled to 110°C over a period of 3 hours in flowing argon. During the reaction, water condenses at the downstream end of the tube furnace. Weight loss during the reaction is about 17-20% of the combined weight of the LiOAc and spinel reactants. The Li^Mn^ spinel powder product is analyzed by atomic absorption (AA) for Li and Mn concentration and characterized by X-ray powder diffraction (XRD) analysis. <br><br>
5 <br><br>
WO 96/40590 <br><br>
Example 2 <br><br>
PCT/US96/09461 <br><br>
( <br><br>
Lithiated spinel of the formula Li1-2Mn204 is prepared from lithium acetate by dissolving 3.39 grams of LiOAc in about 30ml of dionized (DI) water. A stoichiometric amount of particulate LiMn204 spinel, 30 grams, is added to the LiOAc solution and the resulting slurry is stirred to keep the spinel in suspension and to ensure homogeneity between the spinel and LiOAc reactants while heating at 80-90°C for about 3 hours to remove excess water until the slurry turns into a paste. The paste then is vacuum dried at 80°C. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1.5 hours, and is held a:t that temperature for 2 hours to form the Li1.2Mn204 spinel product, a bluish black powder. The powder is cooled to 110°C over a period of 3 hours in flowing argon. During the reaction, water condenses at the downstream end of the tube furnace. The Li1.2MnJ04 spinel powder is characterized by X-ray powder diffraction (XRD) analysis and analyzed by atomic absorption (AA) for Li and Mn concentration to confirm its structure. <br><br>
fifrTOle 3 <br><br>
Lithiated spinel of the formula Li2Mn204 is prepared by dissolving 16.95 grams of lithium acetate (LiOAc) in about 30ml of dionized (DI) water. A stoichiometric amount of particulate LiMn204 spinel, 30 grams, is added to the LiOAc solution and the resulting slurry is stirred to keep the spinel in suspension and the ensure homogeneity between the spinel and LiOAc reactants while the slurry is heated at 80-90°C for about 3 hours to remove <br><br>
6 <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
excess water until the slurry turns into a paste. The paste then is vacuum dried at 80°C. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of l.S hours, and held at that tempeiature for two hours. The powder is cooled to 110°C <br><br>
over a period of 3 hours in flowing argon. During the reaction, <br><br>
water condenses at the downstream end of the furnace. A color change from bluish black to brown is observed during the reaction and the LiaMna04 spinel product has a brown color which is different from the bluish black color of the LiMna04 spinel reactant. The LiaMna04 spinel powder is characterized by X-ray powder diffraction (XRD) analysis and analyzed by atomic absorption (AA) for Li and Mn concentration. <br><br>
Example 4 <br><br>
Lithiated spinel of the formula Lix.!Mna04 is prepared by dissolving 3.482 grams of lithium citrate in about 30ml of deionized water. A stoichiometric amount of LiMna04, 30 grams, is added to the lithium citrate solution and the resulting slurry is stirred to keep the spinel in suspension and to ensure homogeneity between the spinel and lithium citrate reactants. The slurry is heated at 80-90°C for about 3 hours while stirring to remove excess water until the slurry turns into a paste. The paste then is vacuum dried by heating at 80°C for about 3 hours. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1.5 hours and held at that temperature for 2 hours to form a bluish black powder product. The powder then is cooled to 110°C over a period of 3 hours in flowing argon. During the reaction, water is seen condensing at the downstream end of the <br><br>
7 <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
flowing tube furnace. Weight loss during the reaction is about <br><br>
40-45% of the combined weight of the citrate and spinel reactants. The powder is characterized by XRD and analyzed by atomic absorption (AA) for Li and Mn concentration to confirm its structure as Li1.1MnJ04 spinel. <br><br>
Example 5 <br><br>
Lithiated LiliaMna04 spinel is prepared by dissolving 6.964 grams of lithium citrate in about 30ml of deionized water. A stoichiometric amount of LiMn204, 30 grams, is added to the lithium citrate solution and the resulting slurry is stirred to keep the spinel in suspension and to ensure homogeneity between the spinel and lithium citrate reactants. The slurry then is heated at 80-90°C for about 3 hours while stirring to remove excess water until the slurry turns into a paste. The paste is vacuum dried by heating at 80°C for a few hours. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1.5 hours and held at that temperature for 2 hours to form a powder product. The powder is cooled to 110°C over a period of 3 hours in flowing argon. During the reaction, water is seen condensing at the downstream end of the flowing tube furnace. A color change from bluish black to brown is observed during the reaction and the powder product has a brown color which is different from the bluish black color of the LiMna04 spinel reactant. The powder product is characterized by XRD and analyzed for Li and Mn concentration to confirm its structure as Li1.2Mn204 spinel. <br><br>
8 <br><br>
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PCT/US96/09461 <br><br>
Example 6 <br><br>
Lithiated spinel of the formula Li5Mn204 is prepared by dissolving ^4.82 grams of lithium citrate in about 30ml of w <br><br>
deionized water. A stoichiometric amount of particulate LiMn204 spinel, 30 grams, is added to the lithium citrate solution and the resulting slurry is stirred to keep the spinel in suspension and to ensure homogeneity between the spinel and lithium citrate reactants while the slurry is heated at 80-90°C for about 3 hours to remove excess water until the slurry turns into a paste. The paste then is vacuum dried at 80°C. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1.5 hours, and held at that temperature for 2 hours to form a powder product. The powder is cooled to 110°C over a period of 3 hours in flowing argon. During the reaction, water is condensed at the downstream end of the tube furnace. A color change from bluish black to brown is observed during the reaction and the powder product has a brown color which is different from the bluish black color of the LiMn204 spinel reactant. The powder product is characterized by X-ray powder diffraction (XRD) analysis and analyzed by atomic absorption (AA) for Li and Mn concentration to confirm its structure as Li2Mn204 spinel. <br><br>
Example 7 <br><br>
Lithiated Li^Mn^ spinel is prepared by dissolving 1.591 grams of lithium lactate in about 30ml of deionized (DI) water. A stoichiometric amount of particulate LiMn204 spinel, 30 grams, is added to the LiOAc solution and the resulting slurry is <br><br>
9 <br><br>
WO 96/40590 PCT/US96/09461 <br><br>
stirred to keep the spinel in suspension and to' ensure homogeneity between the spinel and LiOAc reactants while heating at 80-90C for about 3 hours to remove excess water until the slurry turns into a paste. The paste is vacuum dried at 80°C. <br><br>
The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1 hour and held at that temperature for 2 hours to form a bluish black powder product. The powder is cooled to <br><br>
110°C over a period of 3 hours in flowing argon. During the reaction, water condenses at the downstream end of the tube furnace. Weight loss during the reaction is about 20% of the combined weight of the lithium lactate and spinel reactants. <br><br>
The powder product is characterized by X-ray powder diffraction <br><br>
(XRD) analysis and analyzed by atomic absorption (AA) for Li and <br><br>
Mn concentration to confirm its structure as Li^MnaO,, spinel. <br><br>
Example 8 <br><br>
Lithiated Lix.2Mn204 spinel is prepared from lithium lactate by dissolving 3.182 grams of lithium lactate in about 30ml of deionized (DI) water. A stoichiometric amount of particulate LiMn204 spinel, 30 grams, is added to the LiOAc solution and the resulting slurry is stirred to keep the spinel in suspension and tj ensure homogeneity between the spinel and LiOAc reactants while the slurry is heated at 80-90°C for about 3 hours to remove excess water until the slurry turns into a paste. The paste then is vacuum dried at 80°C. The resulting powder is slowly heated, in a tube furnace in the presence of flowing argon, from room temperature to 250°C over a period of 1 hour, and held at that temperature for 2 hours to form a bluish black powder product. The powder is cooled to 110°C over a period of 3 hours <br><br>
10 <br><br></p>
</div>
Claims (12)
1. A process for preparing a lithiated lithium manganese dioxide spinel compound of the formula Li,1+X)Mn204 wherein 0<x<l, comprising reacting lithium manganese dioxide spinel compound of the formula LiMn204 with a lithium carboxylate at a temperature and for a time sufficient to decompose said carboxylate and form the lithiated spinel.<br><br>
2. The process of Claim 1 wherein the lithium carboxylate is selected from the group consisting of lithium acetate, lithium citrate, lithium lactate, and other lithium carboxylates in which the carboxylate group is attached to a group that is electron-withdrawing relative to methyl.<br><br>
3. The process of Claim 2 wherein the lithium carboxylate is lithium acetate.<br><br>
4. The process of Claim 1 wherein the reaction takes place at a temperature between about 150°C to below about 350°C.<br><br>
5. The process of Claim 4 wherein the temperature ranges from about 150°C to below about 300°C.<br><br>
6. The process of Claim 1 wherein the time of reaction ranges from about 10 minutes to about 15 hours.<br><br>
7. The process of Claim 5 wherein the time of reaction ranges from about 2 to about 8 hours.<br><br> 12<br><br> 310242<br><br> WO 96/40590 PCT/US96/09461<br><br>
8. The process of Claim 1 wherein the reaction is condu'cted in an inert atmosphere.<br><br>
9. The process of Claim l wherein the lithium manganese dioxide spinel compound is reacted with lithium acetate at a temperature o£ about 230°C to about 250°C for a period of about 2 to about 8 hours in an inert argon atmosphere.<br><br>
10. A process as claimed in claim 1 substantially as herein described.<br><br>
11. A process of producing a lithiated spinel compound substantially in accordance with any one of examples 1 to 9.<br><br>
12. A lithiated lithium manganese dioxide spinel compound of the formula Li(ltx,Mn204 ,wherein 0<x<l, prepared according to the prdcess of Claim 1.<br><br> END OF CLAIMS<br><br> 13<br><br> INTELLECTUAL PROPERTY OFFICE OF N.Z.<br><br> 0 9 OCT IS98 RECEIVED<br><br> </p> </div>
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/474,806 US5693307A (en) | 1995-06-07 | 1995-06-07 | Process for making a lithiated lithium manganese oxide spinel |
| PCT/US1996/009461 WO1996040590A1 (en) | 1995-06-07 | 1996-06-05 | An improved process for making a lithiated lithium manganese oxide spinel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NZ310242A true NZ310242A (en) | 1998-11-25 |
Family
ID=23885010
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NZ310242A NZ310242A (en) | 1995-06-07 | 1996-06-05 | Process for making a lithiated lithium manganese oxide spinel by contacting a lithium magnesium oxide spinel and a lithium carboxylate compound |
Country Status (19)
| Country | Link |
|---|---|
| US (1) | US5693307A (en) |
| EP (1) | EP0842120B1 (en) |
| JP (1) | JPH11507320A (en) |
| KR (1) | KR19990022253A (en) |
| CN (1) | CN1084305C (en) |
| AT (1) | ATE231823T1 (en) |
| AU (1) | AU716975B2 (en) |
| BG (1) | BG62395B1 (en) |
| BR (1) | BR9609184A (en) |
| CA (1) | CA2221738C (en) |
| CZ (1) | CZ371797A3 (en) |
| DE (1) | DE69626023T2 (en) |
| NZ (1) | NZ310242A (en) |
| PL (1) | PL324489A1 (en) |
| RO (1) | RO115348B1 (en) |
| RU (1) | RU2152355C1 (en) |
| TW (1) | TW362090B (en) |
| WO (1) | WO1996040590A1 (en) |
| ZA (1) | ZA963655B (en) |
Families Citing this family (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0797263A2 (en) * | 1996-03-19 | 1997-09-24 | Mitsubishi Chemical Corporation | Nonaqueous electrolyte secondary cell |
| IT1283968B1 (en) * | 1996-03-29 | 1998-05-07 | Consiglio Nazionale Ricerche | RECHARGEABLE LITHIUM OR LITHIUM-ION BATTERY ABLE TO SUSTAIN PROLONGED CYCLING. |
| US6869547B2 (en) * | 1996-12-09 | 2005-03-22 | Valence Technology, Inc. | Stabilized electrochemical cell active material |
| US6183718B1 (en) * | 1996-12-09 | 2001-02-06 | Valence Technology, Inc. | Method of making stabilized electrochemical cell active material of lithium manganese oxide |
| US6110442A (en) * | 1997-05-30 | 2000-08-29 | Hughes Electronics Corporation | Method of preparing Lix Mn2 O4 for lithium-ion batteries |
| US6455198B1 (en) | 1997-11-10 | 2002-09-24 | Ngk Insulators, Ltd. | Lithium secondary battery with a lithium manganese oxide positive electrode |
| US5939043A (en) * | 1998-06-26 | 1999-08-17 | Ga-Tek Inc. | Process for preparing Lix Mn2 O4 intercalation compounds |
| US6468695B1 (en) | 1999-08-18 | 2002-10-22 | Valence Technology Inc. | Active material having extended cycle life |
| JP2001266874A (en) * | 2000-03-16 | 2001-09-28 | Toho Titanium Co Ltd | Lithium ion secondary battery |
| KR101352836B1 (en) * | 2010-10-27 | 2014-01-20 | 전남대학교산학협력단 | Process for Preparing Lithium Manganese-Based Oxide of Li-excess Content and Lithium Secondary Battery Comprising the Same |
| JP5765179B2 (en) * | 2011-10-14 | 2015-08-19 | 日産自動車株式会社 | Positive electrode material for electrochemical device and electrochemical device using the same |
| KR101383681B1 (en) * | 2011-11-15 | 2014-04-10 | 전남대학교산학협력단 | Method for preparing lithium manganese oxides electrode materials, lithium manganese oxides electrode materials prepared thereby and rechargeable battery comprising the electrode materials |
| RU2591154C1 (en) * | 2015-09-03 | 2016-07-10 | Федеральное государственное бюджетное учреждение науки Институт общей и неорганической химии им. Н.С. Курнакова Российской академии наук (ИОНХ РАН) | Method of producing lithiated double lithium and manganese oxide with spinel structure |
| CN105977471A (en) * | 2016-07-06 | 2016-09-28 | 福建师范大学 | Method for improving performance of spinel lithium-rich lithium manganate positive electrode material by use of acid salt |
| CN112960814A (en) * | 2021-02-03 | 2021-06-15 | 中环国投(重庆)环保产业开发有限公司 | Harmless treatment method for leachate of electrolytic manganese slag |
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| US4070529A (en) * | 1976-07-07 | 1978-01-24 | Agence Nationale De Valorisation De La Recherche (Anvar) | Solid electrolyte |
| US4246253A (en) * | 1978-09-29 | 1981-01-20 | Union Carbide Corporation | MnO2 derived from LiMn2 O4 |
| US4312930A (en) * | 1978-09-29 | 1982-01-26 | Union Carbide Corporation | MnO2 Derived from LiMn2 O4 |
| AU532635B2 (en) * | 1979-11-06 | 1983-10-06 | South African Inventions Development Corporation | Metal oxide cathode |
| US4507371A (en) * | 1982-06-02 | 1985-03-26 | South African Inventions Development Corporation | Solid state cell wherein an anode, solid electrolyte and cathode each comprise a cubic-close-packed framework structure |
| US4959282A (en) * | 1988-07-11 | 1990-09-25 | Moli Energy Limited | Cathode active materials, methods of making same and electrochemical cells incorporating the same |
| CA1331506C (en) * | 1988-07-12 | 1994-08-23 | Michael Makepeace Thackeray | Method of synthesizing a lithium manganese oxide |
| GB2234233B (en) * | 1989-07-28 | 1993-02-17 | Csir | Lithium manganese oxide |
| CA2022898C (en) * | 1989-08-15 | 1995-06-20 | Nobuhiro Furukawa | Non-aqueous secondary cell |
| JP2933645B2 (en) * | 1989-08-28 | 1999-08-16 | 日立マクセル株式会社 | Manufacturing method of lithium secondary battery |
| JPH03225750A (en) * | 1990-01-30 | 1991-10-04 | Bridgestone Corp | Positive electrode sheet for lithium battery |
| GB2242898B (en) * | 1990-04-12 | 1993-12-01 | Technology Finance Corp | Lithium transition metal oxide |
| US5166012A (en) * | 1990-05-17 | 1992-11-24 | Technology Finance Corporation (Proprietary) Limited | Manganese oxide compounds |
| JP3028582B2 (en) * | 1990-10-09 | 2000-04-04 | ソニー株式会社 | Non-aqueous electrolyte secondary battery |
| JPH04169065A (en) * | 1990-10-31 | 1992-06-17 | Mitsubishi Electric Corp | Manufacture of positive electrode material for lithium battery |
| US5244757A (en) * | 1991-01-14 | 1993-09-14 | Kabushiki Kaisha Toshiba | Lithium secondary battery |
| US5196279A (en) * | 1991-01-28 | 1993-03-23 | Bell Communications Research, Inc. | Rechargeable battery including a Li1+x Mn2 O4 cathode and a carbon anode |
| US5266299A (en) * | 1991-01-28 | 1993-11-30 | Bell Communications Research, Inc. | Method of preparing LI1+XMN204 for use as secondary battery electrode |
| US5262255A (en) * | 1991-01-30 | 1993-11-16 | Matsushita Electric Industrial Co., Ltd. | Negative electrode for non-aqueous electrolyte secondary battery |
| US5135732A (en) * | 1991-04-23 | 1992-08-04 | Bell Communications Research, Inc. | Method for preparation of LiMn2 O4 intercalation compounds and use thereof in secondary lithium batteries |
| JP3145748B2 (en) * | 1991-11-14 | 2001-03-12 | 富士写真フイルム株式会社 | Organic electrolyte secondary battery |
| US5192629A (en) * | 1992-04-21 | 1993-03-09 | Bell Communications Research, Inc. | High-voltage-stable electrolytes for Li1+x Mn2 O4 /carbon secondary batteries |
| ZA936168B (en) * | 1992-08-28 | 1994-03-22 | Technology Finance Corp | Electrochemical cell |
| US5425932A (en) * | 1993-05-19 | 1995-06-20 | Bell Communications Research, Inc. | Method for synthesis of high capacity Lix Mn2 O4 secondary battery electrode compounds |
| US5478672A (en) * | 1993-12-24 | 1995-12-26 | Sharp Kabushiki Kaisha | Nonaqueous secondary battery, positive-electrode active material |
-
1995
- 1995-06-07 US US08/474,806 patent/US5693307A/en not_active Expired - Lifetime
-
1996
- 1996-05-08 ZA ZA963655A patent/ZA963655B/en unknown
- 1996-05-24 TW TW085106148A patent/TW362090B/en active
- 1996-06-05 CN CN96195030A patent/CN1084305C/en not_active Expired - Fee Related
- 1996-06-05 CA CA002221738A patent/CA2221738C/en not_active Expired - Fee Related
- 1996-06-05 BR BR9609184A patent/BR9609184A/en not_active Application Discontinuation
- 1996-06-05 KR KR1019970708732A patent/KR19990022253A/en not_active Ceased
- 1996-06-05 NZ NZ310242A patent/NZ310242A/en unknown
- 1996-06-05 PL PL96324489A patent/PL324489A1/en unknown
- 1996-06-05 AU AU61004/96A patent/AU716975B2/en not_active Ceased
- 1996-06-05 DE DE69626023T patent/DE69626023T2/en not_active Expired - Fee Related
- 1996-06-05 CZ CZ973717A patent/CZ371797A3/en unknown
- 1996-06-05 EP EP96918315A patent/EP0842120B1/en not_active Expired - Lifetime
- 1996-06-05 RU RU98100422/12A patent/RU2152355C1/en not_active IP Right Cessation
- 1996-06-05 RO RO97-02251A patent/RO115348B1/en unknown
- 1996-06-05 WO PCT/US1996/009461 patent/WO1996040590A1/en not_active Ceased
- 1996-06-05 AT AT96918315T patent/ATE231823T1/en not_active IP Right Cessation
- 1996-06-05 JP JP9501775A patent/JPH11507320A/en active Pending
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1998
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Also Published As
| Publication number | Publication date |
|---|---|
| RO115348B1 (en) | 2000-01-28 |
| CN1084305C (en) | 2002-05-08 |
| KR19990022253A (en) | 1999-03-25 |
| BR9609184A (en) | 1999-05-11 |
| CA2221738A1 (en) | 1996-12-19 |
| RU2152355C1 (en) | 2000-07-10 |
| JPH11507320A (en) | 1999-06-29 |
| EP0842120A4 (en) | 1998-12-09 |
| TW362090B (en) | 1999-06-21 |
| CZ371797A3 (en) | 1998-06-17 |
| BG62395B1 (en) | 1999-10-29 |
| WO1996040590A1 (en) | 1996-12-19 |
| AU6100496A (en) | 1996-12-30 |
| DE69626023D1 (en) | 2003-03-06 |
| US5693307A (en) | 1997-12-02 |
| AU716975B2 (en) | 2000-03-09 |
| HK1010866A1 (en) | 1999-07-02 |
| CN1189143A (en) | 1998-07-29 |
| BG102161A (en) | 1998-08-31 |
| EP0842120B1 (en) | 2003-01-29 |
| EP0842120A1 (en) | 1998-05-20 |
| ATE231823T1 (en) | 2003-02-15 |
| ZA963655B (en) | 1996-11-21 |
| PL324489A1 (en) | 1998-05-25 |
| CA2221738C (en) | 2001-02-27 |
| DE69626023T2 (en) | 2003-10-16 |
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