WO1999040029A1 - Verfahren zur herstellung von lithium-übergangsmetallaten - Google Patents

Verfahren zur herstellung von lithium-übergangsmetallaten Download PDF

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Publication number
WO1999040029A1
WO1999040029A1 PCT/EP1998/005150 EP9805150W WO9940029A1 WO 1999040029 A1 WO1999040029 A1 WO 1999040029A1 EP 9805150 W EP9805150 W EP 9805150W WO 9940029 A1 WO9940029 A1 WO 9940029A1
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WIPO (PCT)
Prior art keywords
compound
transition metal
lithium
calcination
manganese
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Ceased
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PCT/EP1998/005150
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German (de)
English (en)
French (fr)
Inventor
Mathias Benz
Wolfgang Kummer
Evelyn Pross
Josef Schmoll
Wolfgang Schweda
Daniel Duff
Ricarda Leiberich
Christoph Schild
Ulrich Krynitz
Juliane Meese-Marktscheffel
Viktor Stoller
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HC Starck GmbH
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HC Starck GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from PCT/EP1998/000697 external-priority patent/WO1998037023A1/de
Priority to EP98945239A priority Critical patent/EP1058673B1/de
Priority to AU92622/98A priority patent/AU744558B2/en
Priority to DE59811208T priority patent/DE59811208D1/de
Priority to CA002320155A priority patent/CA2320155C/en
Priority to KR1020007008659A priority patent/KR100544541B1/ko
Priority to US09/601,946 priority patent/US6875416B1/en
Priority to AT98945239T priority patent/ATE264271T1/de
Priority to HK01105761.5A priority patent/HK1034952B/xx
Priority to HU0100690A priority patent/HUP0100690A3/hu
Priority to JP2000530464A priority patent/JP4122710B2/ja
Application filed by HC Starck GmbH filed Critical HC Starck GmbH
Priority to IL13735098A priority patent/IL137350A0/xx
Publication of WO1999040029A1 publication Critical patent/WO1999040029A1/de
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/80Compounds containing nickel, with or without oxygen or hydrogen, and containing one or more other elements
    • C01G53/82Compounds containing nickel, with or without oxygen or hydrogen, and containing two or more other elements
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
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    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G45/00Compounds of manganese
    • C01G45/12Complex oxides containing manganese and at least one other metal element
    • C01G45/1221Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof
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    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G45/00Compounds of manganese
    • C01G45/12Complex oxides containing manganese and at least one other metal element
    • C01G45/1221Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof
    • C01G45/1228Manganates or manganites with trivalent manganese, tetravalent manganese or mixtures thereof of the type (MnO2)-, e.g. LiMnO2 or Li(MxMn1-x)O2
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    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G51/00Compounds of cobalt
    • C01G51/40Complex oxides containing cobalt and at least one other metal element
    • C01G51/42Complex oxides containing cobalt and at least one other metal element containing alkali metals, e.g. LiCoO2
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G51/00Compounds of cobalt
    • C01G51/40Complex oxides containing cobalt and at least one other metal element
    • C01G51/42Complex oxides containing cobalt and at least one other metal element containing alkali metals, e.g. LiCoO2
    • C01G51/44Complex oxides containing cobalt and at least one other metal element containing alkali metals, e.g. LiCoO2 containing manganese
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    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G51/00Compounds of cobalt
    • C01G51/80Compounds containing cobalt, with or without oxygen or hydrogen, and containing one or more other elements
    • C01G51/82Compounds containing cobalt, with or without oxygen or hydrogen, and containing two or more other elements
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/40Complex oxides containing nickel and at least one other metal element
    • C01G53/42Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/40Complex oxides containing nickel and at least one other metal element
    • C01G53/42Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2
    • C01G53/44Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese
    • C01G53/50Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection 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
    • HELECTRICITY
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    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/5825Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D15/00Lithium compounds
    • C01D15/10Nitrates
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    • C01G53/00Compounds of nickel
    • C01G53/40Complex oxides containing nickel and at least one other metal element
    • C01G53/42Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2
    • C01G53/44Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese
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    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
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    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/74Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by peak-intensities or a ratio thereof only
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    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
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    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer
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    • C01P2006/40Electric properties
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    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
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    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/485Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present invention relates to a method for producing lithium transition metallates of the general formula
  • M 1 denotes nickel, cobalt or manganese
  • M 2 denotes a transition metal different from M 1 and means chromium, cobalt, iron, manganese, molybdenum and / or aluminum,
  • n 2 if M 1 is manganese and n is 1 if M 1 is nickel or cobalt, where
  • x assumes a value from 0.9 to 1.2
  • y takes a value between 0.5 and 1 and
  • z assumes a value between 1.9 and 2.1.
  • Such lithium transition metallates are used as electrode material, in particular as cathode material, for non-aqueous lithium secondary battery systems, so-called lithium-ion batteries.
  • LiCoO 2 has prevailed in recent years, but due to the limited availability and the associated high price of cobalt it is extremely expensive and is therefore out of the question for mass production (e.g. for the electric drive of vehicles). Therefore, there have already been intensive efforts to use LiCoO 2 as cathode material, for example using LiNiO 2 and / or
  • LiMn 2 ⁇ 4 to replace in whole or in part.
  • the intimate mixture is prepared by coprecipitating soluble lithium and transition metal salts from the solution, drying the solution and calcining.
  • relatively finely divided crystals of the lithium transition metallates are obtained at comparatively low calcination temperatures and within comparatively short times.
  • Lithium transition metalates are formed by solid diffusion during the calcination. Solid-state diffusion requires comparatively high temperatures with comparatively long calcination times and generally did not lead to phase-pure lithium metallates with excellent electronic properties. Extensive observations seem to prove that in the case of the nickel system, a longer temperature treatment above 700 ° C begins to decompose LiNiO 2 with the formation of Li O and NiO.
  • EP-A 0 468 942 has therefore already proposed starting with powdery nickel oxide or hydroxide in the production of lithium nickelate, suspending the powder in a saturated lithium hydroxide solution and removing the water from the suspension by spray drying. This should reduce the calcination time and temperature. Because of the relatively low solubility of lithium hydroxide in water, the homogeneity of this mixture is limited.
  • the transition metal compound is used in the form of a powder with a specific surface area of at least 10 m 2 / g (BET), the transition metal ver - Impregnation bond with a large specific surface area before the calcination with the solution of an oxygen-containing lithium compound and the solvent is removed by drying.
  • the transition metal compound powder is able to absorb the lithium compound in such a way that a continuous phase cannot form when heated to a temperature above the melting point of the lithium compound, and the transition metal compound powders coated with the lithium compound both stick with the reactor wall as well as the powder particles with each other is largely avoided.
  • the present invention accordingly relates to a process for the preparation of lithium transition metallates of the general formula Li ⁇ MiyM 2 !. ⁇ ,, where
  • M 1 denotes nickel, cobalt or manganese
  • M 2 is chromium, cobalt, iron, manganese, molybdenum or aluminum and is not equal to M 1 ,
  • n 2 if M 1 is manganese, otherwise 1
  • y is a number between 0.5 and 1.0
  • z is a number between 1.9 and 2.1
  • Lithium compound and drying was obtained, which is characterized in that at least the M 1 compound is used in the form of a powder with a specific surface area of at least 10 m 2 / g (BET) and the calcination is carried out in a moving bed.
  • the Mi compound preferably has a specific surface area of at least 25 m 2 / g, particularly preferably at least 40 m 2 / g.
  • the hydroxides are used as preferred transition metal compounds M 1 .
  • Nickel hydroxide is particularly preferred.
  • ⁇ -Nickel hydroxide with a specific surface area of 60 to 80 m 2 / g is very particularly preferably used, in particular one which is obtainable according to US Pat. No. 5,391,265.
  • the M 2 transition metal compound is preferably at least partially used in the form of a mixed hydroxide of the formula (M 1 y M 2 1. Y ) (OH) 2 .
  • Y should preferably be greater than 0.8, particularly preferably greater than 0.9.
  • Lithium hydroxide and / or lithium nitrate can be used as the oxygen-containing lithium compound. These are preferably mixed with the transition metal compound in aqueous solution and then dried and granulated. Lithium nitrate is used as the preferred oxygen-containing lithium compound.
  • the aqueous solution of the lithium compound is preferably used in concentrated form, in the case of lithium nitrate as a more than 35% aqueous solution.
  • At least part of the M 2 transition metal compound can be used as a solution component of the solution of the lithium compound for impregnating the M 1 transition metal compound.
  • the solid powdery transition metal compound is mixed with the solution of the lithium compound with stirring and then the solvent, in particular water, is dried by spray drying, fluidized bed spray granulation or mixer agglomeration.
  • the solvent in particular water
  • a spray-dried material with an agglomerate size of less than 100 ⁇ m is preferred.
  • the subsequent calcination in a moving bed can be carried out in a rotary kiln, in a fluidized bed or in a chute reactor (downer).
  • a rotary kiln is particularly preferred.
  • the granules are introduced continuously or batchwise into a preferably electrically heated rotary kiln and for a residence time of 0.5 to 10 hours, preferably 1 to 5 hours, at a temperature of 500 to 800 ° C., preferably 550 to 650 ° C. , particularly preferably 580 to 620 ° C, treated. - 7 -
  • the temperature range from below the melting temperature of the lithium compound to the calcination temperature should be passed as quickly as possible. Accordingly, the intimate mixture is introduced into the rotary kiln which is already at the calcining temperature or into the moving bed which is at the calcining temperature.
  • the intimate mixture can be preheated to a temperature of up to 200 ° C., preferably 150 to 180 ° C.
  • the preheating can be carried out up to a temperature of 350 ° C.
  • the calcination can be carried out in an atmosphere containing up to 50% oxygen, for example air. Calcination is preferred, at least for two thirds of the calcination time, under essentially oxygen-free inert gas, for example argon, with an oxygen content of less than 5%, in particular less than 3%. In this case, calcination is preferably carried out under an oxygen-containing gas atmosphere during the remaining calcination time.
  • the atmosphere can be exchanged for an oxygen-containing atmosphere after at least two thirds of the calcination time.
  • an oxygen-containing atmosphere or oxygen is preferably introduced into the furnace in the last third of the furnace by means of a lance.
  • the lithium transition metallate emerging in powder form from the moving bed is cooled to room temperature (below 100 ° C.) and subjected to gentle grinding.
  • Suitable grinding devices are, for example, those which take advantage of the shear effect of high gas velocity profiles, the size reduction being carried out by particle-particle impact, such as fluidized bed counter-jet mills or micro-vortex mills.
  • the grinding is preferably carried out (after separation of the fine fraction) up to an average grain size of 15 to 25 ⁇ m in diameter.
  • the fine fraction of the grinding is either returned to the moving bed or mixed with the powdery, oxygen-containing transition metal compound and then treated and dried together with the solution of the oxygen-containing lithium compound, i.e. impregnated.
  • Lithium nitrate is particularly preferably used as the oxygen-containing lithium compound.
  • the NO x gas released in this case during the calcination is preferably absorbed in an aqueous lithium hydroxide solution and the resulting lithium nitrate solution is used to impregnate the powdery transition metal compounds.
  • the premix preparation A consists of a stirred container in which a 40% aqueous lithium nitrate solution is placed, into which powdered ⁇ -nickel hydroxide with an average particle size of 10 ⁇ m and a specific surface area of 65 m 2 / g is stirred. The received
  • Slurry is dried by spray drying and introduced into rotary kiln B as granules with an average particle diameter of about 100 ⁇ m.
  • the furnace material is preferably kept under an inert gas at sintering temperature for 1 to 3 hours.
  • the argon atmosphere can then be replaced (in batch mode) by an atmosphere containing 20 to 50% oxygen. Then the
  • the rotary kiln was cooled and the lithium nickelate obtained was ground in a fluidized bed counter-jet mill C to a particle diameter below 40 ⁇ m and the fine fraction with particle sizes below 3 ⁇ m separated by sighting or in a cyclone and collected for return to oven B.
  • the furnace atmosphere containing NO x is washed in a scrubber D with aqueous lithium hydroxide solution and the lithium nitrate obtained is obtained for the renewed premix production.
  • BET is stirred into an approximately 40% aqueous solution of lithium nitrate.
  • the molar ratio of LiNO 3 to Ni (OH) 2 is 1.03.
  • the suspension is dried in a spray tower.
  • the dried powder with an average grain size of about 60 ⁇ m is mixed with 5% by weight lithium nickelate with a grain size ⁇ 5 ⁇ m.
  • 500 g of the powder mixture are placed in the hot zone of a laboratory rotary kiln heated to 620 ° C, through which a stream of nitrogen flows at a speed of 84 m / h.
  • the rotary kiln has an inner diameter of 55 mm and is rotated at 1/4 rpm.
  • the rotary kiln After one hour the rotary kiln is cooled to less than 100 ° C and samples are taken from the oven.
  • Example 1 was repeated with the difference that the rotary kiln is kept at 600 ° C. and the cooling takes place after two hours. - 11 -
  • Example 2 was repeated, first annealing at 640 ° C. under nitrogen and then 30 minutes at 640 ° C. in air.
  • Half-width 003 reflex 0.17
  • Half-width 004-reflex 0.19

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Battery Electrode And Active Subsutance (AREA)
PCT/EP1998/005150 1998-02-09 1998-08-13 Verfahren zur herstellung von lithium-übergangsmetallaten Ceased WO1999040029A1 (de)

Priority Applications (11)

Application Number Priority Date Filing Date Title
IL13735098A IL137350A0 (en) 1998-02-09 1998-08-13 Method for producing lithium-transition metal mixtures
AT98945239T ATE264271T1 (de) 1998-02-09 1998-08-13 Verfahren zur herstellung von lithium- übergangsmetallaten
DE59811208T DE59811208D1 (de) 1998-02-09 1998-08-13 Verfahren zur herstellung von lithium-übergangsmetallaten
CA002320155A CA2320155C (en) 1998-02-09 1998-08-13 Process for preparing lithium transition metallates
KR1020007008659A KR100544541B1 (ko) 1998-02-09 1998-08-13 리튬-전이 금속 혼합물의 제조 방법
US09/601,946 US6875416B1 (en) 1998-02-09 1998-08-13 Method for producing lithium-transition metal mixtures
HU0100690A HUP0100690A3 (en) 1998-02-09 1998-08-13 Method for producing lithium-transition metal mixtures
EP98945239A EP1058673B1 (de) 1998-02-09 1998-08-13 Verfahren zur herstellung von lithium-übergangsmetallaten
HK01105761.5A HK1034952B (en) 1998-02-09 1998-08-13 Method for producing lithium-transition metal mixtures
JP2000530464A JP4122710B2 (ja) 1998-02-09 1998-08-13 リチウム−遷移金属混合物の調製法
AU92622/98A AU744558B2 (en) 1998-02-09 1998-08-13 Method for producing lithium-transition metal mixtures

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
PCT/EP1998/000697 WO1998037023A1 (de) 1997-02-19 1998-02-09 Verfahren zur herstellung von lithium-übergangsmetallaten
EPPCT/EP98/00697 1998-02-09

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WO1999040029A1 true WO1999040029A1 (de) 1999-08-12

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PCT/EP1998/005150 Ceased WO1999040029A1 (de) 1998-02-09 1998-08-13 Verfahren zur herstellung von lithium-übergangsmetallaten

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US (1) US6875416B1 (https=)
EP (1) EP1058673B1 (https=)
JP (1) JP4122710B2 (https=)
KR (1) KR100544541B1 (https=)
CN (1) CN1191994C (https=)
AT (1) ATE264271T1 (https=)
AU (1) AU744558B2 (https=)
CA (1) CA2320155C (https=)
DE (1) DE59811208D1 (https=)
HU (1) HUP0100690A3 (https=)
IL (1) IL137350A0 (https=)
WO (1) WO1999040029A1 (https=)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004034489A3 (en) * 2002-09-13 2005-03-03 Max Planck Ges Zur Novel electrodes for li-based electrochemical energy storage devices and a li-based electrochemical storage device
CN1300868C (zh) * 2003-04-30 2007-02-14 杨永平 锂离子电池用结构稳定的尖晶石锰酸锂的制备方法
US7648693B2 (en) 2005-04-13 2010-01-19 Lg Chem, Ltd. Ni-based lithium transition metal oxide
EP2463942A1 (en) 2006-05-10 2012-06-13 LG Chem, Ltd. Material for lithium secondary battery of high performance
US8426066B2 (en) 2005-04-13 2013-04-23 Lg Chem, Ltd. Material for lithium secondary battery of high performance
US8450013B2 (en) 2005-04-13 2013-05-28 Lg Chem, Ltd. Material for lithium secondary battery of high performance
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CN1191994C (zh) 2005-03-09
HUP0100690A3 (en) 2005-03-29
AU9262298A (en) 1999-08-23
HUP0100690A1 (hu) 2001-06-28
JP4122710B2 (ja) 2008-07-23
EP1058673B1 (de) 2004-04-14
EP1058673A1 (de) 2000-12-13
KR20010040770A (ko) 2001-05-15
DE59811208D1 (de) 2004-05-19
CA2320155A1 (en) 1999-08-12
AU744558B2 (en) 2002-02-28
CN1284932A (zh) 2001-02-21
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