JPH029722A - Production of manganese oxide powder - Google Patents
Production of manganese oxide powderInfo
- Publication number
- JPH029722A JPH029722A JP63159188A JP15918888A JPH029722A JP H029722 A JPH029722 A JP H029722A JP 63159188 A JP63159188 A JP 63159188A JP 15918888 A JP15918888 A JP 15918888A JP H029722 A JPH029722 A JP H029722A
- Authority
- JP
- Japan
- Prior art keywords
- manganese
- manganese oxide
- oxide powder
- droplets
- compd
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G45/00—Compounds of manganese
- C01G45/02—Oxides
-
- 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
-
- 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
- H01M4/502—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese for non-aqueous cells
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/50—Solid solutions
- C01P2002/52—Solid solutions containing elements as dopants
- C01P2002/54—Solid solutions containing elements as dopants one element only
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/30—Particle morphology extending in three dimensions
- C01P2004/32—Spheres
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/51—Particles with a specific particle size distribution
-
- 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
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/40—Electric properties
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
【発明の詳細な説明】
C産業上の利用分野コ
本発明はマンガン酸化物粉末の製造方法に関し、さらに
詳しくは、例え、ぼりチウム二次電池用正極活物質等に
用いられる、充填性、分散性に優れた球状のマンガン酸
化物粉末の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing manganese oxide powder, and more specifically, for example, to improve filling properties and dispersion of manganese oxide powder, which is used as a positive electrode active material for lithium secondary batteries. The present invention relates to a method for producing spherical manganese oxide powder with excellent properties.
[従来技術および発明が解決しようとする課題]現在、
マンガン酸化物粉末を得るためには、電気分解により得
られたマンガン酸化物やマンガン化合物を酸化して得ら
れた不定形のマンガン酸化物を機械的に粉砕し、分級捕
塵する方法が一般的である。[Prior art and problems to be solved by the invention] Currently,
In order to obtain manganese oxide powder, the general method is to mechanically crush the amorphous manganese oxide obtained by oxidizing manganese oxide or manganese compound obtained by electrolysis, and then classify and collect the dust. It is.
しかし、前述の方法では工程が繁雑であるばかりか、捕
集マンガン酸化物の収率が低く、不純物が多く、また形
状が球状でなく不定形のため充填性が低い等の欠点があ
る。However, the above-mentioned method has drawbacks such as not only complicated steps but also a low yield of collected manganese oxide, a large amount of impurities, and low filling properties because the shape is not spherical but amorphous.
このように粉砕、分級したしたマンガン酸化物粉末では
、形状が不定形であるため、充填性が悪く、リチウム二
次電池正極材等に使用した場合、その性能が制限され、
また製造コストが高く、上述のように不純物が多い等の
課題もあった。Since the manganese oxide powder that has been crushed and classified in this way has an amorphous shape, it has poor filling properties, and when used as a positive electrode material for lithium secondary batteries, its performance is limited.
Further, there were also problems such as high manufacturing cost and a large amount of impurities as mentioned above.
本発明は上記のような状況に鑑み、品質、物性を低下さ
せることのない、球状である充填性の良好なマンガン酸
化物粉末の製造方法を提供することを目的としたもので
ある。In view of the above circumstances, the present invention aims to provide a method for producing manganese oxide powder that is spherical and has good filling properties without degrading quality and physical properties.
[課題を解決するための手段]
本発明者らは上記目的を達成するために鋭意研究の結果
、マンガン化合物の水溶液を噴霧器を用いて液滴にして
噴霧し、空気中で熱分解することによって得られる球状
のマンガン酸化物粉末は、従来の製造方法によって得ら
れるマンガン酸化物と比較して、充填性、分散性に優れ
ることを知見して本発明に到達した。[Means for Solving the Problems] In order to achieve the above object, the present inventors have conducted intensive research and found that by spraying an aqueous solution of a manganese compound into droplets using a sprayer and thermally decomposing them in the air. The present invention was achieved based on the finding that the obtained spherical manganese oxide powder has superior filling properties and dispersibility compared to manganese oxide powder obtained by conventional manufacturing methods.
すなわち本発明は、マンガン化合物の水溶液を噴霧17
、得られた液滴を加熱することを特徴とする球状マンガ
ン酸化物粉末の製造方法にある。That is, the present invention provides spraying 17 of an aqueous solution of a manganese compound.
, a method for producing spherical manganese oxide powder, characterized by heating the obtained droplets.
以下、本発明の製造方法について説明する。The manufacturing method of the present invention will be explained below.
本発明では出発原料とし′でマンガン化合物を用いるが
、マンガン化合物としては主に硝酸マンガン、炭酸マン
ガンが用いられるが、他に硫酸マンガン・、塩化マンガ
ン等を用いてもよい。これら原料マンガン化合物を純水
等に溶解してマンガン化合物の水溶液とする。この際の
マンガン濃度は50〜400g/i程度が望ましい。In the present invention, a manganese compound is used as a starting material. Manganese nitrate and manganese carbonate are mainly used as the manganese compound, but manganese sulfate, manganese chloride, etc. may also be used. These raw manganese compounds are dissolved in pure water or the like to obtain an aqueous solution of the manganese compound. The manganese concentration at this time is preferably about 50 to 400 g/i.
また、本発明においては、このマンガン化合物の水溶液
に水酸化リチウム、炭酸リチウム、硝酸リチウム等のリ
チウム化合物を溶解してもよい。Further, in the present invention, a lithium compound such as lithium hydroxide, lithium carbonate, or lithium nitrate may be dissolved in the aqueous solution of the manganese compound.
この際のマンガン濃度は50〜300gz#程度が望ま
しい。このようなリチウム化合物を添加することにより
、マンガン酸化物の中にリチウムイオンが最も拡散し易
くなってくる。The manganese concentration at this time is preferably about 50 to 300 gz#. By adding such a lithium compound, lithium ions can most easily diffuse into the manganese oxide.
本発明では、このマンガン化合物の水溶液を噴霧器を用
いて噴霧し、液滴を得る。ここに用いられる噴霧器とし
ては、特に限定はされないが、例えば超音波噴霧器等が
例示される。In the present invention, this aqueous solution of the manganese compound is sprayed using a sprayer to obtain droplets. The sprayer used here is not particularly limited, but examples include, for example, an ultrasonic sprayer.
次に、得られた液滴を加熱して球状の二酸化マンガンま
たはマンガンとリチウムの複合酸化物を得る。加熱処理
条件としては150〜900”C11〜5分が適当であ
る。Next, the obtained droplets are heated to obtain spherical manganese dioxide or a composite oxide of manganese and lithium. Appropriate heat treatment conditions are 150-900''C11-5 minutes.
このような液滴の加熱に用いられる装置としては、第1
図に示されるような加熱装置が一例として示される。同
図において、1は超音波加湿器、2は反応管、3は電気
炉、4は温度コントローラー 5は捕集器、6は水、7
は吸引ファンをそれぞれ示す。The first device used for heating such droplets is
A heating device as shown in the figure is shown by way of example. In the figure, 1 is an ultrasonic humidifier, 2 is a reaction tube, 3 is an electric furnace, 4 is a temperature controller, 5 is a collector, 6 is water, and 7
indicates a suction fan, respectively.
[作用]
本発明の作用効果は十分に解明されていないが、推定す
るに、以下のことに起因するものと考えられる。[Effects] Although the effects of the present invention have not been fully elucidated, they are presumed to be due to the following factors.
■ 焼結がなく球状り1分散であるため充填性が良好で
ある。■ Since there is no sintering and only spherical particles are dispersed, the filling property is good.
■ 組成が均一で不純物が少ない。■ Uniform composition with few impurities.
本発明はこれら各作用の相乗効果により、充填性、分散
性に優れる高純度の球状のマンガン酸化物が得られるの
である。In the present invention, a highly pure spherical manganese oxide with excellent filling properties and dispersibility can be obtained by the synergistic effect of these respective actions.
[実施例]
以下、本発明を実施例および比較例に基づき具体的に説
明する。[Examples] The present invention will be specifically described below based on Examples and Comparative Examples.
実施例1
硝酸マンガンを純水に溶解して、マンガン濃度−64,
5g / Jの水溶液を得て、この水溶液を噴霧速度1
d/分で噴霧し、得られだ液滴を第1図に示した装置に
より 500℃で1分間加熱し、第2図の顕微鏡写真(
X 3000)に示されるような球状のマンガン酸化物
粉末を得た。Example 1 Manganese nitrate was dissolved in pure water to give a manganese concentration of -64,
5g/J aqueous solution was obtained, and this aqueous solution was sprayed at a spray rate of 1
The droplets obtained were heated at 500°C for 1 minute using the apparatus shown in Figure 1, and the micrograph shown in Figure 2 (
A spherical manganese oxide powder as shown in (X 3000) was obtained.
得られたマンガン酸化物粉末の物性値を第1表に示すと
共に、その粒径および充填度合を第2表にそれぞれ示し
た。The physical properties of the obtained manganese oxide powder are shown in Table 1, and the particle size and filling degree are shown in Table 2.
なお、第1表中の粒度分布とは日機装製粒度測定器マイ
クロトラック SPA型を用いてn1定したものであり
、粒径の小さい方から篩分けして全重量のl0150.
90%の各重量になる寸前の粒径を表示したものである
。Note that the particle size distribution in Table 1 is determined by n1 using a Nikkiso particle size analyzer Microtrac SPA type, and the particle size is sieved from the smallest particle size to 10150.
The particle size just before reaching 90% of each weight is displayed.
また、粉末の充填度合は、電池性能に及ぼす要因とされ
るもので、次の方法により測定した。Further, the degree of filling of powder is considered to be a factor affecting battery performance, and was measured by the following method.
充填度合−光透過法による粒径(μ)/空気透過法によ
る粒径(μ)
上式中、光透過法による粒径は、島津遠心沈11式粒度
分布測定装置を用いて光透過法により測定した粒度分布
の中心値の粒径であり、空気透過法による粒径は、島津
粉体比表面桔測定装置5S−100型を用いて空気透過
法により測定した粒度分布の中心値の粒径である。Filling degree - Particle size by light transmission method (μ) / Particle size by air transmission method (μ) In the above formula, the particle size by light transmission method is determined by light transmission method using a Shimadzu centrifugal sedimentation type 11 particle size distribution analyzer. This is the particle size at the center value of the measured particle size distribution, and the particle size measured by the air permeation method is the particle size at the center value of the particle size distribution measured by the air permeation method using a Shimadzu powder specific surface measurement device model 5S-100. It is.
実施例2
実施例1と同様の方法で液滴を得て、第1図のような加
熱装置により 700℃で1分間加熱し、第3図の顕微
鏡写、Q (X 3000)に示されるような球状のマ
ンガン酸化物粉末を得た。Example 2 Droplets were obtained in the same manner as in Example 1, and heated at 700°C for 1 minute using the heating device shown in Figure 1, resulting in a droplet as shown in the micrograph Q (X 3000) in Figure 3. A spherical manganese oxide powder was obtained.
実施例1と同様に得られたマンガン酸化物粉末の物性値
を第1表に示すと共に、その粒径および充填度合を第2
表にそれぞれ示した。The physical properties of the manganese oxide powder obtained in the same manner as in Example 1 are shown in Table 1, and the particle size and filling degree are shown in Table 2.
Each is shown in the table.
実施例3
炭酸マンガンを過剰の濃硝酸に溶解した溶液に水酸化リ
チウム水溶液を添加し、マンガン濃度−84,5g /
J 、リチウム濃度−3,3g/jの水溶液を得て、
この水溶液を噴霧速度IItl/分で噴霧し、得られた
液滴を前記の装置により 500℃で1分間加熱し、第
4図の顕微鏡写真(X 3000)に示されるような球
状のマンガン酸化物粉末を得た。Example 3 A lithium hydroxide aqueous solution was added to a solution of manganese carbonate dissolved in excess concentrated nitric acid, and the manganese concentration was -84.5 g/
J, an aqueous solution with a lithium concentration of -3.3 g/j was obtained,
This aqueous solution was sprayed at a spray rate of IItl/min, and the resulting droplets were heated at 500°C for 1 minute using the above-mentioned device to form spherical manganese oxides as shown in the micrograph (X 3000) in Figure 4. A powder was obtained.
実施例1と同様に得られたマンガン酸化物粉末の物性値
を第1表に示すと共に、その粒径および充填度合を第2
表にそれぞれ示した。The physical properties of the manganese oxide powder obtained in the same manner as in Example 1 are shown in Table 1, and the particle size and filling degree are shown in Table 2.
Each is shown in the table.
比較例1
電解法によって得られた電解二酸化マンガンを機械的に
粉砕した後、これを分級し、第5図の顕微鏡写g (x
3000)に示されるような形状の二酸化マンガン粉
末を得た。Comparative Example 1 After mechanically pulverizing electrolytic manganese dioxide obtained by electrolytic method, it was classified and the micrograph g (x
3000) was obtained.
実施例1と同様に得られたマンガン酸化物粉末の粒径お
よび充填度合を第2表に示した。The particle size and filling degree of the manganese oxide powder obtained in the same manner as in Example 1 are shown in Table 2.
第
表
第1〜2表から明らかなように、実施例1〜3のマンガ
ン酸化物粉末は、粒度分布が小さく、また比較例1と比
較して充填度合が大きい。As is clear from Tables 1 and 2, the manganese oxide powders of Examples 1 to 3 have a small particle size distribution and a large filling degree compared to Comparative Example 1.
また、第2〜5図に示されるように、比較例1で得られ
るマンガン酸化物粉末が不定形状であるのに対し、実施
例1〜3のマンガン酸化物粉末は球状を示している。Moreover, as shown in FIGS. 2 to 5, the manganese oxide powder obtained in Comparative Example 1 has an irregular shape, whereas the manganese oxide powder of Examples 1 to 3 has a spherical shape.
従って、実施例1〜3のマンガン酸化物粉末は、充填性
、分散性に優れていることが判る。Therefore, it can be seen that the manganese oxide powders of Examples 1 to 3 have excellent filling properties and dispersibility.
[発明の効果]
以上の説明から明らかなように、本発明の製造方法によ
り得られるマンガン酸化物粉末は球状で充填性、分散性
に優れていることから、リチウム二次電池用正極活物質
等の広範な用途に使用可能である。[Effects of the Invention] As is clear from the above description, the manganese oxide powder obtained by the production method of the present invention is spherical and has excellent filling properties and dispersibility, so it can be used as a positive electrode active material for lithium secondary batteries, etc. It can be used for a wide range of applications.
第1図は、本発明に係る加熱工程で用いられる加熱装置
の一例を示す概略図、そして、第2〜5図は、実施例1
〜3および比較例1により得られたマンガン酸化物粉末
の顕微鏡写真(x 3000)をそれぞれ示す。
1;音波加湿器
2;反応管
3:電気炉
4:温度コン
5:捕集機
6:水
7:吸引ファン
トローラー
特許出願人 三井金属鉱業株式会社
代理人 弁理士 伊 東 辰 雄
代理人 弁理士 伊 東 哲 也
* 2 FXIJ < az :3ooO(e
>第
図
(有ト亭・3000倍ン
第 3 肉 (#1亭3α℃倍)
第
図
(脩傘:3COO倍)
手続補正書(方式)
%式%
1、事件の表示
昭和63年 特 許 願 第 159188号2、発明
の名称
マンガン酸化物粉末の製造方法
3、補正をする者
事件との関係 特許出願人
住 所 東京都中央区日本橋室町2丁目1番1号名 称
(618) 三井金属鉱業株式会社代表者 真島公
三部
4、代理人〒105
住 所 東京都港区虎ノ門二丁目8番1号6、補正の対
象
「明細書の図面の簡単な説明の欄」
7、補正の内容
1、明細書第10頁第20行の“顕微鏡写真″を示す顕
微鏡写真」に訂正する。
を
「粒子構造
」FIG. 1 is a schematic diagram showing an example of a heating device used in the heating process according to the present invention, and FIGS. 2 to 5 are example 1
3 and Comparative Example 1 are shown respectively. 1; Sonic humidifier 2; Reaction tube 3: Electric furnace 4: Temperature converter 5: Collector 6: Water 7: Suction fan troller Patent applicant: Mitsui Mining & Mining Co., Ltd., agent, patent attorney Tatsuo Ito, agent, patent attorney Tetsuya Ito* 2 FXIJ < az :3ooO(e
>Figure (Aritutei/3000 times 3rd meat (#1 bow 3α℃ times) Figure (Shukase: 3COO times) Procedural amendment (method) % formula % 1. Indication of the case 1988 Patent Application No. 159188 2, Name of the invention Method for manufacturing manganese oxide powder 3, Relationship to the case of the person making the amendment Patent applicant address 2-1-1 Nihonbashi Muromachi, Chuo-ku, Tokyo Name (618) Mitsui Kinzoku Mining Co., Ltd. Representative Kosanbu Mashima 4, Agent 105 Address 2-8-1-6 Toranomon, Minato-ku, Tokyo Target of amendment: “Brief description of drawings in the specification” 7. Contents of amendment 1. Correct “Microphotograph indicating “Microphotograph” on page 10, line 20 of the specification.” to “Particle structure.”
Claims (1)
加熱することを特徴とするマンガン酸化物粉末の製造方
法。 2、前記マンガン化合物の水溶液中にリチウム化合物を
溶解する請求項1に記載のマンガン酸化物粉末の製造方
法。[Claims] 1. A method for producing manganese oxide powder, which comprises heating droplets obtained by spraying an aqueous solution of a manganese compound. 2. The method for producing manganese oxide powder according to claim 1, wherein a lithium compound is dissolved in the aqueous solution of the manganese compound.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63159188A JPH029722A (en) | 1988-06-29 | 1988-06-29 | Production of manganese oxide powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63159188A JPH029722A (en) | 1988-06-29 | 1988-06-29 | Production of manganese oxide powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH029722A true JPH029722A (en) | 1990-01-12 |
Family
ID=15688237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63159188A Pending JPH029722A (en) | 1988-06-29 | 1988-06-29 | Production of manganese oxide powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH029722A (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02109260A (en) * | 1988-10-18 | 1990-04-20 | Matsushita Electric Ind Co Ltd | Positive electrode for lithium secondary batteries |
| WO1994021560A1 (en) * | 1993-03-17 | 1994-09-29 | Ultralife Batteries (Uk) Limited | Lithiated manganese oxide |
| WO1995009449A1 (en) * | 1993-09-27 | 1995-04-06 | Arthur D. Little, Inc. | Small particle electrodes by aerosol process |
| GB2276155B (en) * | 1993-03-17 | 1996-05-01 | Dowty Electronic Components | Lithiated manganese oxide |
| WO1996022943A1 (en) * | 1995-01-26 | 1996-08-01 | Japan Metals And Chemicals Co., Ltd. | PROCESS FOR PRODUCING SPINEL LiMn2O¿4? |
| US5742070A (en) * | 1993-09-22 | 1998-04-21 | Nippondenso Co., Ltd. | Method for preparing an active substance of chemical cells |
| KR100220865B1 (en) * | 1997-04-01 | 1999-09-15 | 박지만 | Refining method of waste manganese oxide |
| US5958362A (en) * | 1996-03-28 | 1999-09-28 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Method of producing active material powder for lithium secondary battery |
| US6383235B1 (en) * | 1997-09-26 | 2002-05-07 | Mitsubishi Denki Kabushiki Kaisha | Cathode materials, process for the preparation thereof and secondary lithium ion battery using the cathode materials |
| US6770226B2 (en) * | 1998-02-24 | 2004-08-03 | Superior Micropowders | Fine powders for use in primary and secondary batteries |
| US7181792B2 (en) | 2003-08-08 | 2007-02-27 | Hitachi, Ltd. | Radiotherapeutic bed apparatus |
| JP2011090859A (en) * | 2009-10-22 | 2011-05-06 | Univ Of Fukui | Manufacturing method of lithium ion secondary battery cathode active material |
| JP2011210536A (en) * | 2010-03-30 | 2011-10-20 | Dainippon Printing Co Ltd | Manufacturing method of electrode active material |
| EP1268054B1 (en) * | 2000-03-22 | 2012-12-05 | Cabot Corporation | Method for producing electrocatalyst powders |
| CN102942224A (en) * | 2012-11-10 | 2013-02-27 | 吉林大学 | Synthesis method for rock salt mine MnS nano-cuboid superlattice |
| CN111348685A (en) * | 2020-03-02 | 2020-06-30 | 新奥石墨烯技术有限公司 | Graphene-based composite material, preparation method and application thereof |
| JP2021064581A (en) * | 2019-10-17 | 2021-04-22 | 住友金属鉱山株式会社 | Positive electrode active material for lithium ion secondary battery and manufacturing method thereof |
-
1988
- 1988-06-29 JP JP63159188A patent/JPH029722A/en active Pending
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02109260A (en) * | 1988-10-18 | 1990-04-20 | Matsushita Electric Ind Co Ltd | Positive electrode for lithium secondary batteries |
| WO1994021560A1 (en) * | 1993-03-17 | 1994-09-29 | Ultralife Batteries (Uk) Limited | Lithiated manganese oxide |
| GB2276155B (en) * | 1993-03-17 | 1996-05-01 | Dowty Electronic Components | Lithiated manganese oxide |
| US5683835A (en) * | 1993-03-17 | 1997-11-04 | Ultralife Batteries (Uk) Limited | Lithiated manganese oxide |
| US5742070A (en) * | 1993-09-22 | 1998-04-21 | Nippondenso Co., Ltd. | Method for preparing an active substance of chemical cells |
| WO1995009449A1 (en) * | 1993-09-27 | 1995-04-06 | Arthur D. Little, Inc. | Small particle electrodes by aerosol process |
| US5589300A (en) * | 1993-09-27 | 1996-12-31 | Arthur D. Little, Inc. | Small particle electrodes by aerosol process |
| WO1996022943A1 (en) * | 1995-01-26 | 1996-08-01 | Japan Metals And Chemicals Co., Ltd. | PROCESS FOR PRODUCING SPINEL LiMn2O¿4? |
| US5807532A (en) * | 1995-01-26 | 1998-09-15 | Japan Metals And Chemicals Co., Ltd. | Method of producing spinel type limn204 |
| US5958362A (en) * | 1996-03-28 | 1999-09-28 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Method of producing active material powder for lithium secondary battery |
| KR100220865B1 (en) * | 1997-04-01 | 1999-09-15 | 박지만 | Refining method of waste manganese oxide |
| US6383235B1 (en) * | 1997-09-26 | 2002-05-07 | Mitsubishi Denki Kabushiki Kaisha | Cathode materials, process for the preparation thereof and secondary lithium ion battery using the cathode materials |
| US6770226B2 (en) * | 1998-02-24 | 2004-08-03 | Superior Micropowders | Fine powders for use in primary and secondary batteries |
| EP1268054B1 (en) * | 2000-03-22 | 2012-12-05 | Cabot Corporation | Method for producing electrocatalyst powders |
| US7181792B2 (en) | 2003-08-08 | 2007-02-27 | Hitachi, Ltd. | Radiotherapeutic bed apparatus |
| JP2011090859A (en) * | 2009-10-22 | 2011-05-06 | Univ Of Fukui | Manufacturing method of lithium ion secondary battery cathode active material |
| JP2011210536A (en) * | 2010-03-30 | 2011-10-20 | Dainippon Printing Co Ltd | Manufacturing method of electrode active material |
| CN102942224A (en) * | 2012-11-10 | 2013-02-27 | 吉林大学 | Synthesis method for rock salt mine MnS nano-cuboid superlattice |
| JP2021064581A (en) * | 2019-10-17 | 2021-04-22 | 住友金属鉱山株式会社 | Positive electrode active material for lithium ion secondary battery and manufacturing method thereof |
| CN111348685A (en) * | 2020-03-02 | 2020-06-30 | 新奥石墨烯技术有限公司 | Graphene-based composite material, preparation method and application thereof |
| CN111348685B (en) * | 2020-03-02 | 2023-01-10 | 新奥集团股份有限公司 | Graphene-based composite material and its preparation method and application |
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