WO2011136497A2 - 리튬 전이금속 인산염의 제조방법 - Google Patents
리튬 전이금속 인산염의 제조방법 Download PDFInfo
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- WO2011136497A2 WO2011136497A2 PCT/KR2011/002816 KR2011002816W WO2011136497A2 WO 2011136497 A2 WO2011136497 A2 WO 2011136497A2 KR 2011002816 W KR2011002816 W KR 2011002816W WO 2011136497 A2 WO2011136497 A2 WO 2011136497A2
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/10—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/45—Phosphates containing plural metal, or metal and ammonium
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- 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
- H01M4/58—Selection 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
- H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/04—Particle morphology depicted by an image obtained by TEM, STEM, STM or AFM
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
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- 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
Definitions
- Lithium transition metal phosphate (LiMPO 4 : M is a transition metal, hereinafter referred to as LMP) is a material that is expected to be used as a positive electrode active material of a lithium secondary battery.
- the solid phase method is a method for producing LMP by mixing and heat treating a solid phase reaction material.
- the dependence on the reaction material is required because it requires the use of fine reaction materials of several hundred nanometers or less.
- the price competitiveness is low due to the increase.
- the heat treatment itself since the heat treatment itself must also proceed in a reducing atmosphere, special care is required.
- the LMP has a low electrical conductivity due to the nature of the material, it is necessary to coat the conductive material on the surface of the LMP particles in order to implement the battery characteristics, when using a solid-phase method, such a surface coating has a problem.
- the sol-gel method (Sol-Gel) is a method of producing a LMP by gelling the metal alkoxide raw material in a sol state and then condensation reaction, and drying and heat-treating it, the price of the reaction raw materials used is high and organic solvent based Since it is a reaction, manufacturing cost is high.
- One embodiment of the present invention is to inject a reaction raw material containing lithium, transition metal and phosphoric acid into the reactor to mix (mixing at the molecular level) and chemical reaction (chemical reaction) to generate nucleating (nucleating) It provides a method for producing a lithium transition metal phosphate comprising the step.
- It provides a method for producing a lithium transition metal phosphate comprising the step of chemically reacting the reaction raw material in the reactor (nucleating).
- the transition metal may include at least one selected from the group consisting of Fe, Mn, Co, and Ni.
- the chemical reaction may be an acid group reaction.
- the reaction raw material may be injected into the reactor in the form of at least one of a solution form and a suspension form.
- the reaction raw material may include an acidic raw material and a basic raw material, the acidic raw material may be injected into the reactor through a first raw material injection line, and the basic raw material may be injected into the reactor through a second raw material injection line.
- the acidic raw material may include lithium, transition metal and phosphoric acid
- the basic raw material may include an inorganic base.
- the acidic raw material may include a transition metal and phosphoric acid, and the basic raw material may include lithium.
- the acidic raw material may include lithium and phosphoric acid, and the basic raw material may include a transition metal.
- the basic raw material may include lithium and a transition metal
- the acidic raw material may include phosphoric acid
- the time (T M ) required for mixing at the molecular level may be shorter than the time (T N ) required for nucleation.
- the T M may be 10 to 100 ⁇ s, and the T N may be 1 ⁇ m or less.
- the internal temperature of the reactor may be maintained at 0 ⁇ 90 °C.
- the molar ratio of lithium + transition metal to phosphoric acid ((Li + M) / phosphoric acid) in the reaction raw material may be 1.5 ⁇ 2.5.
- the residence time of the reaction raw material in the reactor may be 1ms ⁇ 10s.
- the reactor includes a chamber defining an inner space, a rotatable permeable packed bed disposed in the chamber and filled with a porous filler, and at least one raw material for injecting the reaction raw material into the inner space. It may be a high gravity rotating packed bed reactor having an injection line and a slurry outlet for discharging the slurry from the inner space.
- the reactor may further include a gas outlet for discharging gas from the internal space.
- the porous filler may contain titanium.
- Centrifugal acceleration of the permeable packed layer may be maintained at 10 ⁇ 100,000 m / s 2 .
- the lithium transition metal phosphate may have an olivine type crystal structure.
- a reaction material containing lithium, a transition metal and phosphoric acid is injected into a reactor, mixed at the molecular level and chemical reaction to produce nucleating crystals.
- a method for producing lithium transition metal phosphate which can mass-produce LMP with a uniform particle size distribution and high purity at low cost.
- FIG. 1 is a cross-sectional view schematically showing a high gravity rotary packed bed reactor used in the method for producing lithium transition metal phosphate according to one embodiment of the present invention.
- Example 2 is a TEM photograph of the lithium transition metal phosphate nanoparticles prepared in Example 1 of the present invention.
- Example 3 is an XRD diffraction pattern of the lithium transition metal phosphate nanoparticles prepared in Example 1 of the present invention.
- Figure 4 is a TEM photograph of the lithium transition metal phosphate nanoparticles prepared in Example 2 of the present invention.
- Example 5 is an XRD diffraction pattern of the lithium transition metal phosphate nanoparticles prepared in Example 2 of the present invention.
- Example 6 is a TEM photograph of the lithium transition metal phosphate nanoparticles prepared in Example 3 of the present invention.
- Example 7 is an XRD diffraction pattern of the lithium transition metal phosphate nanoparticles prepared in Example 3 of the present invention.
- Example 8 is a TEM photograph of the lithium transition metal phosphate nanoparticles prepared in Example 4 of the present invention.
- Example 9 is an XRD diffraction pattern of the lithium transition metal phosphate nanoparticles prepared in Example 4 of the present invention.
- Method for producing a lithium transition metal phosphate is a step of injecting a reaction material containing lithium, transition metal and phosphoric acid into the reactor mixing at the molecular level in the reactor (mixing at the molecular level), And chemically reacting the reaction raw materials in the reactor to produce nucleating crystals and growing them to nanoscale. Thereafter, the slurry discharged from the reaction may be filtered, washed, dried and / or heat treated to obtain a uniform nano-sized lithium transition metal phosphate (LMP).
- LMP lithium transition metal phosphate
- 'lithium' means a lithium compound, a lithium atom and / or a lithium ion in some cases
- a 'transition metal' in some cases means a transition metal compound, a transition metal atom and / or a transition metal ion.
- the transition metal may include at least one selected from the group consisting of Fe, Mn, Co, and Ni.
- the "molecular level of mixing” means the level of mixing at which each molecule is mixed.
- 'mixing' can be divided into 'macro-mixing' and 'micro-mixing', where macro mixing means mixing at the vessel scale, Micro mixing is synonymous with mixing at the molecular level described above.
- the reaction raw material may be injected into the reactor in the form of at least one of a solution form and a suspension form.
- the reaction raw material may include an acid raw material and a basic raw material.
- the acidic raw material may be injected into the reactor through a first raw material injection line
- the basic raw material may be injected into the reactor through a second raw material injection line.
- the acidic raw material and the basic raw material are injected into the reactor through the first raw material injection line and the second raw material injection line, respectively, mixed at the molecular level in the reactor, and then subjected to a chemical reaction such as an acid group reaction. LMP nanoparticles are formed.
- the acidic raw material may include lithium, transition metal and phosphoric acid.
- the acidic raw material may include lithium chloride, transition metal chloride and H 3 PO 4 .
- the acidic raw material may be, for example, an aqueous LiCl / FeCl 2 / H 3 PO 4 solution or a water suspension.
- the basic raw material may include an inorganic base such as NH 4 OH.
- the acidic raw material may include a transition metal and phosphoric acid
- the basic raw material may include lithium
- the acidic raw material may include a transition metal chloride such as FeCl 2 and H 3 PO 4
- the basic raw material may include a lithium hydroxide such as LiOH.
- the acidic raw material may include lithium and phosphoric acid
- the basic raw material may include a transition metal.
- the acidic raw material may include lithium chloride such as LiCl and H 3 PO 4
- the basic raw material may include a transition metal hydroxide such as Fe (OH) 2 .
- the basic raw material may include lithium and transition metal.
- the basic raw material may include lithium hydroxide and transition metal hydroxide.
- the basic raw material may be, for example, LiOH / Fe (OH) 2 aqueous solution or water suspension.
- the acidic raw material may include phosphoric acid such as H 3 PO 4 , and optionally other inorganic and organic acids.
- Such lithium chloride, transition metal chloride, lithium hydroxide, transition metal hydroxide and phosphoric acid is low in cost it can reduce the manufacturing cost of lithium transition metal phosphate nanoparticles.
- the chemical reaction may be an acid group reaction in which the acid and the base in the reaction raw material react by one equivalent, thereby losing the properties of the acid and the base.
- the time (T M ) required for mixing at the molecular level may be shorter than the time (T N ) required for nucleation.
- 'T M ' refers to the time taken from the start of mixing until the composition of the mixture becomes spatially uniform
- 'T N ' means that the seed formation rate is in equilibrium from the point where the seed starts to form. It means the time it takes to reach and produce seed at a constant rate.
- T M is controlled to be shorter than T N , when the maximum mixing between molecules is achieved before the start of nucleation in the reactor, LMP particles having a uniform particle size distribution can be prepared.
- the T M may be 10 to 100 ⁇ s, and the T N may be 1 ⁇ m or less. If the T M is less than 10 GPa, it is not preferable from the economical point of view. In addition, when the T N exceeds 1 kPa, an appropriate level of reaction does not occur and thus yield is not preferable.
- the internal temperature of the reactor may be maintained at 0 to 90 ° C., for example, 20 to 80 ° C. If the temperature is less than 0 ° C., an appropriate level of yield cannot be secured, which is not preferable. If the temperature is higher than 90 ° C., T N is difficult to control, which is not preferable.
- the molar ratio ((Li + M) / phosphoric acid) of lithium + transition metal to phosphoric acid in the reaction raw material may be 1.5 ⁇ 2.5.
- metal phosphate secondary phases such as LiFeP 2 O 7 and Fe 4 (P 2 O 7 ) 3 precipitate on the surface of the LMP nanoparticles, and when it exceeds 2.5, Secondary phases, such as Li 2 O, Fe 2 O 3 , Fe 2 P, Li 3 PO 4 and Li 4 P 2 O 7 , are deposited on the surface of the LMP nanoparticles.
- the residence time of the reaction raw material in the reactor may be 1ms ⁇ 10s, for example, 10ms ⁇ 5s. If the residence time of the reaction raw material is less than 1ms is not preferable because the appropriate level of the reaction does not occur, if it exceeds 10s it is difficult to control the particle size of the LMP, it is not economical because it is not preferred.
- FIG. 1 is a schematic cross-sectional view of a high gravity rotating packed bed reactor used in the method for preparing a lithium transition metal phosphate according to an embodiment of the present invention.
- This high gravity rotary packed reactor 10 is a chamber 11 defining an interior space, a rotatable permeable packed bed disposed in the chamber 11 and filled with a porous filler 12a ( 12) at least one raw material injection line (14-1, 14-2) for injecting the reaction raw material into the inner space; And a slurry outlet 15 for discharging the slurry from the inner space.
- the reactor 10 may further include a gas outlet 16 for discharging gas from the internal space.
- Porous filler 12a may contain titanium which is highly corrosion resistant. Specifically, the porous filler 12a may be titanium foam.
- the permeable filler layer 12 is filled with a porous filler 12a therein and transmits the reaction raw material injected into the reactor 10 in the form of a solution or a suspension, and may be rotated by the drive shaft 13.
- the centrifugal acceleration of the permeable filler 12 can be maintained at 10 ⁇ 100,000 m / s 2 . If the centrifugal acceleration of the permeable packed layer 12 is less than 10 m / s 2, the reaction may not proceed to an appropriate level. On the other hand, it is not easy in the reactor design technology that the centrifugal acceleration of the permeable packed layer 12 exceeds 100,000 m / s 2 .
- the reactor 10 having the above configuration is operated under atmospheric pressure, the reaction raw materials can be mixed at a molecular level by a large centrifugal force by controlling the rotational speed of the permeable packed bed 12, so that the reaction proceeds smoothly even at low temperatures. You can. In other words, by uniformly mixing the reaction material of the fine droplets before the growth of the LMP particles, uniform LMP nanoparticles can be obtained at low temperature. Since the reactor 10 is a continuous reactor, it can produce a large amount of LMP.
- the LMP prepared by the method for preparing a lithium transition metal phosphate according to one embodiment of the present invention may have an olivine-type crystal structure, and an average particle diameter thereof may be 0.01 to 10 ⁇ m, for example, 0.05 to 0.8 ⁇ m. . Therefore, the prepared lithium transition metal phosphate may be used as a cathode active material of a lithium secondary battery.
- a reactor 10 similar to the reactor of FIG. 1 was manufactured by itself.
- the specifications of the manufactured reactor 10 were as follows.
- Permeable filling layer (12) stainless steel, inner diameter 10 cm, outer diameter 30 cm, thickness 10 cm cylindrical
- Porous filler (12a) 4 pieces of titanium foam (approximately 400 pores per meter, outer diameter 30cm, inner diameter 10.5cm, axial thickness 2.5cm)
- the drive shaft 13 of the reactor 10 is rotated to rotate the permeable packed bed 12 at a speed of 1440 rpm (central acceleration: 60,000 m / s 2 ) while the reactor 10 ) was maintained at 80 ° C.
- the first raw material injection line 14-1 and the second raw material injection LMP nanoparticles were obtained by continuously injecting the reactor 10 at a flow rate of 30 L / min through the line 14-2.
- the aqueous FeCl 2 and H 3 PO 4 aqueous solution were mixed at a volume ratio of 1: 1. Mixing, maintaining an internal temperature of the reactor at 60 ° C., and mixing the FeCl 2 / H 3 PO 4 mixed solution and the LiOH aqueous solution into the first raw material injection line 14-1 and the second raw material injection line 14-2, respectively.
- LMP nanoparticles were prepared in the same manner as in Example 1, except that the reactor 10 was continuously injected into the reactor 10 at a flow rate of 40 L / min and 10 L / min, and then filtered, washed, and dried. LMP nanoparticles were obtained.
- the ratio of the reaction raw material component is injected in the reactor 10, i.e., H 3 PO 4 over (Li + Fe), the molar ratio ((Li + Fe) / H 3 PO 4) was the second.
- the aqueous LiCl solution and H 3 PO 4 aqueous solution were 1: 1.
- LMP nanoparticles were prepared and filtered in the same manner as in Example 1, except that the reactor 10 was continuously injected at a flow rate of 40 L / min and 20 L / min through line 14-2, respectively.
- the ratio of the reaction raw material component is injected in the reactor 10, i.e., H 3 PO 4 over (Li + Fe), the molar ratio ((Li + Fe) / H 3 PO 4) was the second.
- the LiOH aqueous solution and Fe (OH) 2 aqueous solution were 1: 1. And mixing the volume ratio of the reactor, maintaining the internal temperature of the reactor at 60 ° C., and mixing the H 3 PO 4 aqueous solution and the LiOH / Fe (OH) 2 mixed solution into the first raw material injection line 14-1 and the second, respectively.
- LMP nanoparticles were prepared in the same manner as in Example 1, except that the reactor 10 was continuously injected at a flow rate of 10 L / min and 40 L / min through the raw material injection line 14-2, respectively.
- the ratio of the reaction raw material component is injected in the reactor 10, i.e., H 3 PO 4 over (Li + Fe), the molar ratio ((Li + Fe) / H 3 PO 4) was the second.
- each particle produced is LMP (LiMPO 4 ).
- Each numerical value e.g., 100 nm in Fig. 2 shown in Figs. 2, 4, 6 and 8 means the length of the thick bar shown in each figure, and each numerical value indicated in Figs.
- (111) of FIG. 3 means a crystal plane index.
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Abstract
Description
TEM | XRD | ||
사양 | 제조사 | JEOL | Rikagu |
모델명 | 2100F | D/Max-2500VK/PC | |
분석조건 | 200kV | CuKa radiation, speed 4°min-1 |
Claims (17)
- 리튬, 전이금속 및 인산을 포함하는 반응원료를 반응기에 주입하여 상기 반응기내에서 분자 수준으로 혼합(mixing at the molecular level)하는 단계; 및상기 반응기 내에서 상기 반응원료를 화학반응(chemical reaction)시켜 결정핵을 생성(nucleating)하는 단계를 포함하는 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 전이금속은 Fe, Mn, Co 및 Ni로 이루어진 군으로부터 선택된 적어도 1종을 포함하는 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 화학반응은 산염기 반응인 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 반응원료는 용액 형태 및 현탁액 형태 중 적어도 하나의 형태로 상기 반응기에 주입되는 리튬 전이금속 인산염의 제조방법.
- 제4항에 있어서,상기 반응원료는 산성 원료 및 염기성 원료를 포함하고, 상기 산성 원료는 제1 원료 주입라인을 통해 상기 반응기에 주입되고, 상기 염기성 원료는 제2 원료 주입라인을 통해 상기 반응기에 주입되는 리튬 전이금속 인산염의 제조방법.
- 제5항에 있어서,상기 산성 원료는 리튬, 전이금속 및 인산을 포함하고, 상기 염기성 원료는 무기염기를 포함하는 리튬 전이금속 인산염의 제조방법.
- 제5항에 있어서,상기 산성 원료는 전이금속 및 인산을 포함하고, 상기 염기성 원료는 리튬을 포함하는 리튬 전이금속 인산염의 제조방법.
- 제5항에 있어서,상기 산성 원료는 리튬 및 인산을 포함하고, 상기 염기성 원료는 전이금속을 포함하는 리튬 전이금속 인산염의 제조방법.
- 제5항에 있어서,상기 염기성 원료는 리튬 및 전이금속을 포함하고, 상기 산성 원료는 인산을 포함하는 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 분자 수준의 혼합에 소요되는 시간(TM)은 상기 결정핵 생성에 소요되는 시간(TN) 보다 짧은 리튬 전이금속 인산염의 제조방법.
- 제10항에 있어서,상기 TM은 10~100㎲이고, 상기 TN은 1㎳ 이하인 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 반응기의 내부 온도는 0~90℃로 유지되는 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 반응원료 중 인산에 대한 리튬+전이금속의 몰비((Li+M)/인산)는 1.5~2.5인 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 반응기 내에서 상기 반응원료의 체류시간은 1㎳~10s인 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 반응기는,내부공간을 한정하는 챔버(chamber);상기 챔버내에 배치되고 다공성 충전재가 충전된 회전가능한 투과성 충전층(permeable packed bed);상기 내부공간에 상기 반응원료를 주입하는 적어도 하나의 원료 주입라인; 및상기 내부공간으로부터 슬러리를 배출하는 슬러리 배출구를 구비하는 고중력 회전 충전형 반응기(high gravity rotating packed bed reactor)인 리튬 전이금속 인산염의 제조방법.
- 제15항에 있어서,상기 투과성 충전층의 원심 가속도는 10~100,000m/s2로 유지되는 리튬 전이금속 인산염의 제조방법.
- 제1항에 있어서,상기 리튬 전이금속 인산염은 올리빈형 결정구조(olivine type crystal structure)를 갖는 리튬 전이금속 인산염의 제조방법.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
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JP2013507869A JP5796260B2 (ja) | 2010-04-30 | 2011-04-20 | リチウム遷移金属リン酸塩の製造方法 |
CN201180021860.8A CN102869606B (zh) | 2010-04-30 | 2011-04-20 | 锂过渡金属磷酸盐的制备方法 |
EP11775202.2A EP2565158B1 (en) | 2010-04-30 | 2011-04-20 | Method for manufacturing a lithium transition metal phosphate |
US13/695,342 US9537149B2 (en) | 2010-04-30 | 2011-04-20 | Method for manufacturing a lithium transition metal phosphate |
CA2797831A CA2797831C (en) | 2010-04-30 | 2011-04-20 | Method of manufacturing a lithium transition metal phosphate |
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KR1020100040797A KR101698762B1 (ko) | 2010-04-30 | 2010-04-30 | 리튬 전이금속 인산염의 제조방법 |
KR10-2010-0040797 | 2010-04-30 |
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CN105000541B (zh) * | 2015-07-31 | 2017-12-19 | 浙江大学宁波理工学院 | 一种纳米羟基磷灰石的制备方法 |
CN105344125A (zh) * | 2015-12-08 | 2016-02-24 | 山西长林环保机械设备有限公司 | 一种卧式双进口增压旋转填料床 |
CN116374986A (zh) * | 2023-04-14 | 2023-07-04 | 河南佰利新能源材料有限公司 | 一种磷酸铁锂正极材料及其制备方法和应用 |
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CA2797831C (en) | 2018-06-12 |
WO2011136497A9 (ko) | 2011-12-29 |
US20130045153A1 (en) | 2013-02-21 |
KR101698762B1 (ko) | 2017-01-23 |
CN102869606A (zh) | 2013-01-09 |
JP2013530112A (ja) | 2013-07-25 |
CN102869606B (zh) | 2016-03-02 |
WO2011136497A3 (ko) | 2012-03-01 |
CA2797831A1 (en) | 2011-11-03 |
KR20110121272A (ko) | 2011-11-07 |
EP2565158B1 (en) | 2019-07-31 |
US9537149B2 (en) | 2017-01-03 |
EP2565158A4 (en) | 2016-04-13 |
JP5796260B2 (ja) | 2015-10-21 |
EP2565158A2 (en) | 2013-03-06 |
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