JPH07112929B2 - Synthesis method of lithium manganese oxide solid solution - Google Patents
Synthesis method of lithium manganese oxide solid solutionInfo
- Publication number
- JPH07112929B2 JPH07112929B2 JP62043550A JP4355087A JPH07112929B2 JP H07112929 B2 JPH07112929 B2 JP H07112929B2 JP 62043550 A JP62043550 A JP 62043550A JP 4355087 A JP4355087 A JP 4355087A JP H07112929 B2 JPH07112929 B2 JP H07112929B2
- Authority
- JP
- Japan
- Prior art keywords
- solid solution
- oxide
- lithium
- heating
- manganese oxide
- 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.)
- Expired - Lifetime
Links
Classifications
-
- 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
-
- 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
- H01M4/485—Selection 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
-
- 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)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はリチウムマンガン酸化物固溶体の合成法に関す
る。The present invention relates to a method for synthesizing a lithium manganese oxide solid solution.
最近、LiMnO2(リチウムマンガン酸化物)などのLiMnO2
(リチウム遷移金属酸化物)が高エネルギー密度を期待
できるリチウム電池の正極活物質として注目を受けてい
る。Recently, LiMnO 2, such as LiMnO 2 (lithium manganese oxide)
(Lithium transition metal oxide) is receiving attention as a positive electrode active material for lithium batteries, which can be expected to have high energy density.
しかし、LiMnO2の場合は、供給する酸素の量を反応に必
要な量に限定しながら合成しなければならなかった。こ
れは、LiMnO2の場合、LiCoO2などとは異なり、開放され
た酸化雰囲気で加熱すると、Mn(マンガン)が容易に酸
化されてMn(IV)になり、例えばLiMn2O4などのLiMO2と
異なる結晶構造になるため、供給する酸素量を限定して
Mn(IV)の生成を防止する必要があるからである。However, in the case of LiMnO 2 , it had to be synthesized while limiting the amount of oxygen supplied to the amount required for the reaction. In the case of LiMnO 2 , unlike LiCoO 2, etc., when heated in an open oxidizing atmosphere, Mn (manganese) is easily oxidized to Mn (IV), for example LiMO 2 such as LiMn 2 O 4. Since the crystal structure is different from that of
This is because it is necessary to prevent the generation of Mn (IV).
そのような事情から、これまでは、Li2O2とMnOを真空封
管して、Li2O2の熱分解によって生じるO2のみによりMn
(II)OをMn(III)に酸化してLiMnO2を合成していた
(J.Am.Chem、Soc.,78,3255(1956))。Under such circumstances, until now, Li 2 O 2 and MnO were sealed in a vacuum tube, and Mn was formed only by O 2 generated by thermal decomposition of Li 2 O 2.
(II) O was oxidized to Mn (III) to synthesize LiMnO 2 (J. Am. Chem, Soc., 78 , 3255 (1956)).
しかし、この方法は、真空封管のため、合成に手間がか
かり、またLi2O2という過酸化物を用いるため危険であ
るという問題があった。However, this method has a problem that it takes a lot of time to synthesize it because it is a vacuum sealed tube, and it is dangerous because it uses a peroxide of Li 2 O 2 .
本発明は、従来、LiMnO2の合成に際して真空封管により
供給する酸素量を制限しなければならないという制約を
受けたり、また取扱いにおいても危険を伴ったという事
実に鑑み、例えばリチウム電池を正極活物質として用い
る場合にLiMnO2よりもむしろ有用なリチウムマンガン酸
化物固溶体を前述のような制約や危険性を招くことなく
合成することを目的とする。The present invention has hitherto been limited by the fact that the amount of oxygen supplied by a vacuum sealed tube during the synthesis of LiMnO 2 must be limited, and in view of the fact that handling also involved danger, for example, a lithium battery with a positive electrode active The purpose of the present invention is to synthesize a useful lithium manganese oxide solid solution rather than LiMnO 2 when used as a substance, without causing the above-mentioned restrictions and risks.
本発明は、マンガンの酸化物または加熱により酸化物に
なる塩と、コバルトの酸化物または加熱により酸化物に
なる塩と、リチウムの酸化物または加熱により酸化物に
なる塩とを混合し、酸素供給量を制限しない開放された
雰囲気で加熱することによって、リチウム電池用の正極
活物質としてLiMnO2よりもむしろ有用な、式(I) Li(Mn1-yCoy)O2 (I) (式中、yは0.1以上で1未満である)で示されるリチ
ウムマンガン酸化物固溶体を、供給する酸素量を制限す
ることなく得られるようにしたものである。The present invention is a mixture of a manganese oxide or a salt which becomes an oxide upon heating, an oxide of cobalt or a salt which becomes an oxide upon heating, and an oxide of lithium or a salt which becomes an oxide upon heating to obtain oxygen. The formula (I) Li (Mn 1-y Co y ) O 2 (I) (I) (I) (I) (I) (I) (I), which is useful as a positive electrode active material for lithium batteries rather than LiMnO 2 by heating in an open atmosphere without limiting the supply In the formula, y is 0.1 or more and less than 1), and a lithium manganese oxide solid solution represented by the formula can be obtained without limiting the amount of oxygen supplied.
本発明において、マンガンと、コバルトと、リチウムと
を、それぞれ酸化物または加熱により酸化物になる塩の
状態で反応に供するが、上記加熱により酸化物になる塩
としては、例えば炭酸塩、酢酸塩などがあげられる。特
に炭酸塩の状態で反応に供すると、加熱により脱炭酸
し、その際に微粒子化するので、各反応成分の混合状態
がより一層均一になるので好ましい結果が得られる。な
お、酸化物としては、Mnの場合はMnO、Mn2O3、Mn3O4な
どが用いられ、コバルトの場合はCoO、Co2O3、Co3O4な
どが用いられ、Liの場合はLi2Oなどが用いられる。In the present invention, manganese, cobalt, and lithium are each subjected to a reaction in the state of an oxide or a salt which becomes an oxide by heating. Examples of the salt which becomes an oxide by heating include carbonate and acetate. And so on. In particular, when the reaction is carried out in the carbonate state, it is decarboxylated by heating and atomized at that time, so that the mixed state of each reaction component becomes more uniform, and a preferable result is obtained. As the oxide, in the case of Mn, MnO, Mn 2 O 3 , Mn 3 O 4, etc. are used, in the case of cobalt, CoO, Co 2 O 3 , Co 3 O 4, etc. are used, and in the case of Li Is Li 2 O or the like.
反応は酸素供給量を制限しない開放された雰囲気で行わ
れるが、この酸素供給量を制限しない開放された雰囲気
は、たとえ大気中より酸素が希薄な雰囲気であってもよ
く、むしろコバルトの固溶化量が少なかったり、あるい
は反応温度が低い場合には、上記酸素が希薄な雰囲気の
方が大気中よりも目的とする固溶体をより安定して得る
ことができるという特徴がある。The reaction is carried out in an open atmosphere in which the oxygen supply amount is not restricted, but the open atmosphere in which the oxygen supply amount is not restricted may be an atmosphere in which oxygen is leaner than in the atmosphere, rather, it is a solid solution of cobalt. If the amount is small or the reaction temperature is low, the oxygen-diluted atmosphere is characterized by being able to obtain the desired solid solution more stably than in the atmosphere.
本発明においては、Mnと、コバルトと、リチウムとを、
それぞれ酸化物または加熱により酸化物になる塩の状態
で反応に供するが、このようにコバルトを含ませた3成
分系で反応させることにより、CoがMnと固溶化すること
になって、酸素の供給量を限定しない酸素雰囲気中で加
熱しても、通常の条件下では酸化されやすいMnの価数が
あがらずMn(III)の酸化物が合成されるようになるも
のと考えられる。In the present invention, Mn, cobalt, and lithium,
Each of them is subjected to the reaction in the state of an oxide or a salt that becomes an oxide by heating, but by reacting in a three-component system containing cobalt in this way, Co becomes a solid solution with Mn, It is considered that even if the material is heated in an oxygen atmosphere whose supply amount is not limited, the valence of Mn, which is easily oxidized, does not increase under normal conditions, and the oxide of Mn (III) is synthesized.
上記のようにMnが酸化されにくくなる理由は、現在のと
ころ必ずしも明確ではないが、CoがMnに固溶化すること
により、MnやCoが3価の状態であるLi(Mn1-yCoy)O2の
結晶構造が安定化し、それによってMnも3価の状態でと
どまるようになるからであると考えられる。The reason why Mn is less likely to be oxidized as described above is not always clear at present, but when Co is dissolved in Mn, Mn and Co are in a trivalent state, Li (Mn 1-y Co y ) It is considered that the crystal structure of O 2 is stabilized and Mn also stays in the trivalent state.
本発明において、式(I)中、つまりLi(Mn1-yCoy)O2
中のyの値を0.1以上で1未満(つまり、0.1≦y<1)
にするが、これはyが0.1より小さいと、Mnとコバルト
との固溶化が充分に生じず、したがって、供給する酸素
量を制限しない開放された酸素雰囲気中では、LiMnO2は
もとよりリチウムマンガン酸化物固溶体が得られなくな
るからである。そして、LiCoO2を開放された酸素雰囲気
中で合成しうることから、yは1未満であればその上限
値は存在しないと考えられるからである。In the present invention, in the formula (I), that is, Li (Mn 1-y Co y ) O 2
The value of y is 0.1 or more and less than 1 (that is, 0.1 ≦ y <1)
However, when y is smaller than 0.1, the solid solution of Mn and cobalt does not sufficiently occur, and therefore, in an open oxygen atmosphere where the amount of oxygen supplied is not limited, not only LiMnO 2 but also lithium manganese oxide is oxidized. This is because a solid solution cannot be obtained. Then, since LiCoO 2 can be synthesized in an open oxygen atmosphere, if y is less than 1, it is considered that the upper limit value does not exist.
本発明においては、前述のように、Mnと、コバルトと、
リチウムとを炭酸塩の状態で反応に供することが好まし
いが、この際、Mnとコバルトとは前もって炭酸塩として
共沈させることにより混合しておくことが好ましい。こ
れは共沈させることによって、Mnの炭酸塩とコバルトの
炭酸塩が均一に混合するからである。In the present invention, as described above, Mn, cobalt,
Lithium and carbonate are preferably used in the reaction in the form of a carbonate. At this time, Mn and cobalt are preferably mixed by coprecipitating them as a carbonate in advance. This is because the Mn carbonate and the cobalt carbonate are uniformly mixed by coprecipitation.
なお、上記のように共沈させる場合、得られる炭酸塩
は、特に厳しく管理された条件下でないかぎり、塩基性
炭酸塩となりやすい。それ故、本発明において炭酸塩と
は、塩基性炭酸塩をも含む概念である。When coprecipitated as described above, the obtained carbonate is likely to be a basic carbonate unless under particularly strictly controlled conditions. Therefore, the carbonate in the present invention is a concept including a basic carbonate.
上記のようにMnとコバルトとを水溶液中で炭酸塩として
共沈させるには、例えばMnの水溶性塩(例えば、Mnの塩
化物)とコバルトの水溶性塩(例えば、コバルトの塩化
物)を炭酸ガスを飽和した純水に溶解し、この溶液に例
えばNaHCO3やNa2CO3などの可溶性炭酸塩を加え、それら
を反応させることによって行われる。As described above, for coprecipitating Mn and cobalt as carbonate in an aqueous solution, for example, a water-soluble salt of Mn (for example, chloride of Mn) and a water-soluble salt of cobalt (for example, chloride of cobalt) are used. It is carried out by dissolving carbon dioxide gas in saturated pure water, adding soluble carbonate such as NaHCO 3 or Na 2 CO 3 to this solution, and reacting them.
加熱温度としては、800〜1200℃を採用するのが好まし
いが、これは800℃未満ではMnとコバルトとの固溶化が
起こりにくく、一方、1200℃を超えるとLiの揮発による
損失が多くなって定量的な反応生成物が得られにくくな
るからである。なお、Mnに添加するCoなどのコバルトの
量が多くなると、反応は上記範囲内での温度の低い側で
も確実に実施できるようになる。As the heating temperature, it is preferable to adopt 800 to 1200 ° C, but when it is less than 800 ° C, solid solution of Mn and cobalt hardly occurs, while when it exceeds 1200 ° C, loss due to volatilization of Li increases. This is because it becomes difficult to obtain a quantitative reaction product. When the amount of cobalt such as Co added to Mn increases, the reaction can be reliably performed even on the low temperature side within the above range.
加熱後の冷却は、特に限定されるものではないが、急冷
による方が冷却の間での予定外の相分離(固溶化したも
のが分離する)が生じるおそれがないので好ましい。Cooling after heating is not particularly limited, but rapid cooling is preferable because there is no risk of unplanned phase separation (separated solid solution is separated) during cooling.
本発明においては、得られるリチウムマンガン酸化物固
溶体をLi(Mn1-yCoy)O2で示したが、(Mn1-yCoy)部分
が若干過剰になりLiに対して等量以上(通常5%以下の
範囲で)になる場合もあるし、また、酸素欠陥が生じて
O2の部分がO2−δ、つまりLi(Mn1-yCoy)O
2−δ(δ≦0.3)になることもあるが、本発明におけ
る式(I)で示されるリチウムマンガン酸化物固溶体は
それらの場合も含むものである。In the present invention, the obtained lithium-manganese oxide solid solution is represented by Li (Mn 1-y Co y ) O 2. However, the (Mn 1-y Co y ) portion is slightly excessive and the amount is equal to or more than Li. (Usually in the range of 5% or less), or when oxygen deficiency occurs
O 2 portions O 2-[delta], i.e. Li (Mn 1-y Co y ) O
2-δ (δ ≦ 0.3) may occur, but the lithium-manganese oxide solid solution represented by the formula (I) in the present invention includes those cases.
そして、本発明によって合成される式(I)で示される
リチウムマンガン酸化物固溶体は、リチウム電池の正極
活物質として用いた場合、電池電圧が3.9〜4.6V(Liが
0〜1の範囲で変動するので、それに伴って電池電圧も
変動する)と二硫化チタンや二硫化モリブデンなどの硫
化物系活物質を用いた電池(通常、電池電圧が3V以下)
より高く、高エネルギー密度が期待できる。また、LiMn
O2よりも、例えばLi(Mn1-yCoy)O2では充放電時の分極
が少なく、充放電時の電池電圧の変化が小さくなるの
で、正極活物質としてむしろ有用である。このように分
極が小さくなるのは、Coが固溶化することにより、Li+
イオンの拡散が速くなるためであると考えられる。When the lithium manganese oxide solid solution represented by the formula (I) synthesized by the present invention is used as a positive electrode active material of a lithium battery, the battery voltage is 3.9 to 4.6 V (Li varies in the range of 0 to 1). Battery voltage also fluctuates accordingly) and batteries using sulfide-based active materials such as titanium disulfide and molybdenum disulfide (usually battery voltage is 3 V or less)
Higher and higher energy density can be expected. Also, LiMn
For example, Li (Mn 1-y Co y ) O 2 is more useful than O 2 as a positive electrode active material because it has less polarization during charging / discharging and a smaller change in battery voltage during charging / discharging. The decrease in polarization is due to the solid solution of Co, which causes Li +
It is considered that this is because the diffusion of ions becomes faster.
つぎに実施例をあげて本発明をさらに詳細に説明する。 Next, the present invention will be described in more detail with reference to examples.
実施例1 LiとMnとCoを用い、Li(MnCo)O2固溶体を合成した。Co
とMnとのモル比は10:90(つまり、Co/Mn=10/90(モル
比))である。Example 1 A Li (MnCo) O 2 solid solution was synthesized using Li, Mn, and Co. Co
The molar ratio of Mn to Mn is 10:90 (that is, Co / Mn = 10/90 (molar ratio)).
合成によって得られた固溶体を式(I)にしたがって表
示すると、Li(Mn0.9Co0.1)O2である。The solid solution obtained by the synthesis is represented by the formula (I) and is Li (Mn 0.9 Co 0.1 ) O 2 .
合成方法は次に示すとおりである。The synthetic method is as follows.
まず、MnとCoとがCo/Mn=10/90(モル比)になる割合で
MnCl・4H2OとCoCl2・6H2Oを炭酸ガスを飽和した純水に
溶解し、濃度4重量%のNaHCO3水溶液を加え、2時間放
置して、MnとCoを炭酸塩として共沈させて均一な混合物
とし、得られた沈澱物を濾過、水洗した後、アルゴン中
140℃で5日間乾燥した。First, at the ratio of Mn and Co such that Co / Mn = 10/90 (molar ratio)
MnCl · 4H 2 O and CoCl 2 · 6H 2 O were dissolved in pure water saturated with carbon dioxide gas, a NaHCO 3 aqueous solution with a concentration of 4 wt% was added, and the mixture was allowed to stand for 2 hours to coprecipitate Mn and Co as carbonates. To form a uniform mixture, and the resulting precipitate is filtered and washed with water, then in argon.
It was dried at 140 ° C for 5 days.
つぎに、上記MnとCoとの共沈物とLi2CO3とをモル比1:1
の割合で混合し、空気中(N2/O2=80/20)、1200℃で3
時間加熱したのち、エア・クエンチ(加熱したサンプル
を25℃の大気中に取り出し急冷する方法)することによ
って合成を行った。加熱にあたって試料を収容するのに
使用したポートはAl2O3を主成分とするものである。ま
た、合成温度のみを1000℃に変えて他は上記と同一条件
下での合成も行った。Next, the coprecipitate of Mn and Co and Li 2 CO 3 are mixed at a molar ratio of 1: 1.
Mix in the ratio of 3 and in air (N 2 / O 2 = 80/20) at 1200 ℃
After heating for a period of time, synthesis was performed by air quenching (a method in which a heated sample was taken out into the atmosphere at 25 ° C. and rapidly cooled). The port used for accommodating the sample during heating is mainly composed of Al 2 O 3 . Also, the synthesis was carried out under the same conditions as above except that the synthesis temperature was changed to 1000 ° C.
さらに、上記ではLi2CO3を当量用いて合成を行ったが、
加熱中におけるリチウムの揮発による損失を補うため、
Li2CO3を1.5倍等量仕込んだ合成も行った。Furthermore, in the above, the synthesis was performed using Li 2 CO 3 in an equivalent amount,
To compensate for the loss due to volatilization of lithium during heating,
A synthesis was also performed in which an equivalent amount of Li 2 CO 3 was charged.
実施例2 Co/Mn比を30/70(モル比)とした以外は、実施例1と同
様にしてLi(MnCo)O2固溶体を合成した。合成された固
溶体を式(I)にしたがって表示すると、Li(Mn0.7Co
0.3)O2である。Example 2 A Li (MnCo) O 2 solid solution was synthesized in the same manner as in Example 1 except that the Co / Mn ratio was 30/70 (molar ratio). Displaying the synthesized solid solution according to the formula (I), Li (Mn 0.7 Co
0.3 ) O 2 .
実施例3 Co/Mn比を50/50(モル比)とした以外は、実施例1と同
様にしてLi(MnCo)O2固溶体を合成した。合成された固
溶体を式(I)にしたがって表示すると、Li(Mn0.5Co
0.5)O2である。Example 3 A Li (MnCo) O 2 solid solution was synthesized in the same manner as in Example 1 except that the Co / Mn ratio was changed to 50/50 (molar ratio). Displaying the synthesized solid solution according to the formula (I), Li (Mn 0.5 Co
0.5 ) O 2 .
実施例4 Co/Mn比を70/30(モル比)とした以外は、実施例1と同
様にしてLi(MnCo)O2固溶体を合成した。合成された固
溶体を式(I)にしたがって表示すると、Li(Mn0.3Co
0.7)O2である。Example 4 A Li (MnCo) O 2 solid solution was synthesized in the same manner as in Example 1 except that the Co / Mn ratio was 70/30 (molar ratio). Displaying the synthesized solid solution according to the formula (I), Li (Mn 0.3 Co
0.7 ) O 2 .
実施例5 Co/Mn比を80/20(モル比)とした以外は、実施例1と同
様にしてLi(MnCo)O2固溶体を合成した。合成された固
溶体を式(I)にしたがって表示すると、Li(Mn0.2Co
0.8)O2である。Example 5 A Li (MnCo) O 2 solid solution was synthesized in the same manner as in Example 1 except that the Co / Mn ratio was 80/20 (molar ratio). Displaying the synthesized solid solution according to the formula (I), Li (Mn 0.2 Co
0.8 ) O 2 .
比較例1 Coを固溶させずにCo/Mn比を0/100とした以外は実施例1
と同様にして合成を行った。Comparative Example 1 Example 1 except that Co / Mn ratio was 0/100 without solid solution of Co
Synthesis was performed in the same manner as in.
比較例2 Coを100モル%とし、Co/Mn比を100/0とした以外は実施
例1と同様にして合成を行った。Comparative Example 2 Synthesis was performed in the same manner as in Example 1 except that Co was 100 mol% and the Co / Mn ratio was 100/0.
上記のように合成した実施例1〜5および比較例1〜2
の物質についてX線回折像を測定し、合成した物質の同
定を行った。測定は50kV、150mA、CuターゲットのX線
源を用いて、4゜/minのスキャン速度で2θ=7〜100
゜の範囲を測定することによって行った。その結果を第
1表に示す。Examples 1-5 and Comparative Examples 1-2 synthesized as described above
An X-ray diffraction pattern was measured for the substance (1) to identify the synthesized substance. The measurement was carried out using an X-ray source of 50 kV, 150 mA, Cu target, 2θ = 7-100 at a scan rate of 4 ° / min.
This was done by measuring the range of °. The results are shown in Table 1.
第1表に示すように、Coを添加しなかった比較例1(Co
/Mn=0/100)では、LiMnO2なる物質は合成されず、LiMn
2O4となり、Mnは高い価数まで酸化されていた。 As shown in Table 1, Comparative Example 1 (Co
/ Mn = 0/100), the substance LiMnO 2 was not synthesized,
It became 2 O 4 , and Mn was oxidized to a high valence.
これに対し、Coを少量添加した実施例1(Co/Mn=10/9
0)では、Li(MnCo)O2固溶体となり、Mnの価数は3価
で高くならなかった。On the other hand, Example 1 in which a small amount of Co was added (Co / Mn = 10/9
In (0), it became a Li (MnCo) O 2 solid solution, and the valence of Mn was trivalent and did not increase.
以上のような結果から判断すると、固溶化してLi(Mn
1-yCoy)O2となるためのCoの下限量は、Co/Mn=0/100〜
10/90の間であり、少なくともCo/Mnを10/90(モル比)
にしておけば、酸素雰囲気中でも、目的とする固溶体が
得られると考えられる。Judging from the above results, solid solution occurs and Li (Mn
The lower limit of Co for 1-y Co y ) O 2 is Co / Mn = 0/100 to
Between 10/90 and at least Co / Mn 10/90 (molar ratio)
If so, it is considered that the desired solid solution can be obtained even in an oxygen atmosphere.
Coの添加量を増加した実施例2〜5では、いずれもLi
(Mn1-yCoy)O2となり、またCoを100モル%にした比較
例2でも、LiCoO2が得られたことから、Mnが3価を保ち
得るCoの添加量の上限値は存在しないと考えられる。In Examples 2 to 5 in which the amount of Co added was increased, Li was
(Mn 1-y Co y ) O 2 was obtained, and also in Comparative Example 2 in which Co was 100 mol%, LiCoO 2 was obtained. Therefore, there is an upper limit of the amount of Co that can maintain the trivalence of Mn. It is thought not to.
なお、上記第1表に示す結果は、Li2CO3の仕込量を多く
して加熱中のLiの揮発による損失を補った時のものであ
る。Li2CO3を当量仕込んだ場合は、Co/Mn比50/50よりMn
量の多い実施例1、2、3では、LiMn2O4がわずかなが
ら生じた。これは加熱中にLiが揮発してしまうためと考
えられる。したがって、安定してLi(Mn1-yCo)O2系の
固溶体を得るには、Li2CO3を等量より過剰に用いるのが
好ましいといえる。また、Li2CO3が多くなっても反応上
は特に弊害が生じないと考えられる。The results shown in Table 1 above were obtained when the charged amount of Li 2 CO 3 was increased to compensate for the loss due to volatilization of Li during heating. When the equivalent amount of Li 2 CO 3 is charged, the Mn is 50% from the Co / Mn ratio of 50/50.
In the large amount of Examples 1, 2, and 3, a small amount of LiMn 2 O 4 was generated. This is probably because Li volatilizes during heating. Therefore, in order to stably obtain a Li (Mn 1-y Co) O 2 -based solid solution, it can be said that it is preferable to use Li 2 CO 3 in excess of the equivalent amount. In addition, it is considered that even if the amount of Li 2 CO 3 increases, no particular adverse effect occurs on the reaction.
また、合成温度の下限値は明らかでないが、CoがMnより
等量以上の実施例3〜5では、合成温度を800℃に下げ
ても安定してLi(MnCo)O2固溶体を合成することができ
た。Further, although the lower limit of the synthesis temperature is not clear, in Examples 3 to 5 in which Co is equal to or more than Mn, it is possible to stably synthesize the Li (MnCo) O 2 solid solution even if the synthesis temperature is lowered to 800 ° C. I was able to.
つぎに、六方晶系に属するLi(MnCo)O2固溶体の格子定
数c0、a0をそれぞれ(006)、(110)面のピーク値より
算出した。その結果を第1図に示す。これに使用した試
料は合成温度1200℃で合成されたものである。Next, the lattice constants c 0 and a 0 of the Li (MnCo) O 2 solid solution belonging to the hexagonal system were calculated from the peak values of the (006) and (110) planes, respectively. The results are shown in FIG. The sample used for this was synthesized at a synthesis temperature of 1200 ° C.
第1図に示すように、Co量の増加に伴ってc0、a0はほ直
線的に減少し、均一に固溶していく様子がわかる。これ
は、Co3+のイオン半径がMn3+のイオン半径に比べて0.05
A程小さいことから定量的に説明できる。As shown in FIG. 1, it can be seen that c 0 and a 0 decrease linearly as the amount of Co increases, and that the solid solution uniformly occurs. This is because the ionic radius of Co 3+ is 0.05 compared to that of Mn 3+.
Since it is as small as A, it can be explained quantitatively.
以上説明したように、本発明では、MnにCoを固溶化させ
ることにより、供給する酸素量を限定しない開放された
酸素雰囲気中での反応によって、Li(Mn1-yCoy)O2で示
されるリチウムマンガン酸化物固溶体を容易に合成する
ことができるようになった。これによって従来LiMnO2を
合成するにあたって真空封管により供給する酸素量の制
限をしなければならなかったり、あるいは危険を伴った
などの問題が解決され、リチウム電池の正極活物質とし
てLiMnO2よりもむしろ有用なLiMnO2類似化合物を容易に
合成できるようになった。As described above, in the present invention, by solid solution of Co in Mn, the reaction in an open oxygen atmosphere does not limit the amount of oxygen supplied, Li (Mn 1-y Co y ) O 2 The lithium manganese oxide solid solution shown can now be easily synthesized. As a result, problems such as the fact that the amount of oxygen supplied by a vacuum sealed tube had to be limited when synthesizing LiMnO 2 in the past, or it was accompanied by danger, were solved, and LiMnO 2 was used as a positive electrode active material for lithium batteries rather than LiMnO 2. Rather, useful LiMnO 2 analogues can be easily synthesized.
第1図は本発明により合成したLi(Mn1-yCoy)O2系固溶
体の格子定数a0、c0値を示す図である。FIG. 1 is a diagram showing the lattice constants a 0 and c 0 of the Li (Mn 1-y Co y ) O 2 type solid solution synthesized according to the present invention.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 真辺 俊勝 大阪府茨木市丑寅1丁目1番88号 日立マ クセル株式会社内 (72)発明者 浅井 彪 大阪府高槻市日吉台1番町10番44号 (72)発明者 河合 七雄 大阪府吹田市千里山西5丁目47番20号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshikatsu Manabe 1-88, 1-Tora, Ibaraki-shi, Osaka Prefecture Hitachi Maxell Co., Ltd. No. (72) Inventor Nanao Kawai 5-47-20 Senriyama Nishi, Suita City, Osaka Prefecture
Claims (2)
になる塩と、コバルトの酸化物または加熱により酸化物
になる塩と、リチウムの酸化物または加熱により酸化物
になる塩とを混合し、酸素供給量を制限しない開放され
た雰囲気で加熱して、式(I) Li(Mn1-yCOy)O2 (I) (式中、yは0.1以上で1未満である) で示されるリチウムマンガン酸化物固溶体を合成するこ
とを特徴とするリチウムマンガン酸化物固溶体の合成
法。1. A mixture of an oxide of manganese or a salt which becomes an oxide by heating, an oxide of cobalt or a salt which becomes an oxide by heating, and an oxide of lithium or a salt which becomes an oxide by heating, It is represented by the formula (I) Li (Mn 1-y CO y ) O 2 (I) (wherein y is 0.1 or more and less than 1 ) by heating in an open atmosphere without limiting the oxygen supply amount. A method for synthesizing a lithium manganese oxide solid solution, which comprises synthesizing a lithium manganese oxide solid solution.
である特許請求の範囲第1項記載のリチウムマンガン酸
化物固溶体の合成法。2. The method for synthesizing a lithium-manganese oxide solid solution according to claim 1, wherein the salt which becomes an oxide by heating is a carbonate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62043550A JPH07112929B2 (en) | 1987-02-25 | 1987-02-25 | Synthesis method of lithium manganese oxide solid solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62043550A JPH07112929B2 (en) | 1987-02-25 | 1987-02-25 | Synthesis method of lithium manganese oxide solid solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63210028A JPS63210028A (en) | 1988-08-31 |
| JPH07112929B2 true JPH07112929B2 (en) | 1995-12-06 |
Family
ID=12666863
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62043550A Expired - Lifetime JPH07112929B2 (en) | 1987-02-25 | 1987-02-25 | Synthesis method of lithium manganese oxide solid solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07112929B2 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2703278B2 (en) * | 1988-08-30 | 1998-01-26 | 三洋電機株式会社 | Non-aqueous secondary battery |
| JP2554370B2 (en) * | 1989-01-27 | 1996-11-13 | 富士電気化学株式会社 | Method for manufacturing non-aqueous electrolyte secondary battery |
| JPH0732017B2 (en) * | 1989-10-06 | 1995-04-10 | 松下電器産業株式会社 | Non-aqueous electrolyte secondary battery |
| JPH04267053A (en) * | 1991-02-21 | 1992-09-22 | Yuasa Corp | Lithium secondary battery |
| JPH04282561A (en) * | 1991-03-11 | 1992-10-07 | Matsushita Electric Ind Co Ltd | Nonaqueous electrolyte secondary battery |
| JP2729176B2 (en) * | 1993-04-01 | 1998-03-18 | 富士化学工業株式会社 | Method for producing LiM3 + O2 or LiMn2O4 and LiNi3 + O2 for cathode material of secondary battery |
| JP3550783B2 (en) * | 1994-05-16 | 2004-08-04 | 東ソー株式会社 | Lithium-containing transition metal composite oxide, method for producing the same, and use thereof |
| FR2721308B1 (en) * | 1994-06-21 | 1996-10-11 | Commissariat Energie Atomique | Manganese oxide insertion compounds, usable as a positive electrode in a lithium battery. |
| EP1135334B1 (en) | 1998-11-20 | 2002-10-09 | Fmc Corporation | Multiple doped lithium manganese oxide compounds and methods of preparing same |
| US20070111099A1 (en) * | 2005-11-15 | 2007-05-17 | Nanjundaswamy Kirakodu S | Primary lithium ion electrochemical cells |
-
1987
- 1987-02-25 JP JP62043550A patent/JPH07112929B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63210028A (en) | 1988-08-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3930574B2 (en) | Electrochemical cell | |
| KR100449219B1 (en) | Electrode material for rechargeable batteries and process for the preparation thereof | |
| JP3221352B2 (en) | Method for producing spinel-type lithium manganese composite oxide | |
| Xia et al. | Studies on an Li Mn O spinel system (obtained by melt-impregnation) as a cathode for 4 V lithium batteries part 1. Synthesis and electrochemical behaviour of LixMn2O4 | |
| EP0701535B1 (en) | METHOD FOR SYNTHESIS OF HIGH CAPACITY LixMn2O4 SECONDARY BATTERY ELECTRODE COMPOUNDS | |
| US6248477B1 (en) | Cathode intercalation compositions, production methods and rechargeable lithium batteries containing the same | |
| KR100393739B1 (en) | Lithium secondary battery | |
| EP0915810B1 (en) | Synthesis of lithium nickel cobalt dioxide | |
| US5820790A (en) | Positive electrode for non-aqueous cell | |
| US5980786A (en) | Method for producing a complex oxide used as a cathode active material of a lithium secondary battery | |
| EP0154331A2 (en) | Lithium-manganese dioxide cell | |
| US5948565A (en) | Cathode material for lithium secondary batteries and a process and a precursor material for the production thereof | |
| JPH07112929B2 (en) | Synthesis method of lithium manganese oxide solid solution | |
| JP3707744B2 (en) | Method for producing lithium composite oxide | |
| Chang et al. | Syntheses of LiCoO2 for cathode materials of secondary batteries from reflux reactions at 130–200 C | |
| US6706443B1 (en) | Process for preparing lithium manganese oxides | |
| Manev et al. | Rechargeable lithium battery with spinel-related λ-MnO2 III. Scaling-up problems associated with LiMn2O4 synthesis | |
| JPH05201733A (en) | Manganese dioxide material | |
| EP3767720A1 (en) | Positive electrode active material particles for non-aqueous electrolyte secondary battery and production method therefor, and non-aqueous electrolyte secondary battery | |
| JPH08333120A (en) | Spinel structure containing lithium and manganese (iii/iv) | |
| Santander et al. | Process optimization and electrochemical properties of lithium manganate cathode for rechargeable batteries | |
| JP3407594B2 (en) | Method for producing lithium nickel composite oxide | |
| JP3331373B2 (en) | Positive electrode material for lithium secondary battery, method for producing the same, and lithium secondary battery using the positive electrode material | |
| JP4774661B2 (en) | Lithium transition metal composite oxide, positive electrode material for lithium secondary battery, positive electrode for lithium secondary battery and lithium secondary battery, and method for producing lithium transition metal composite oxide | |
| JPH082921A (en) | Lithium manganese composite oxide, method for producing the same, and use thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |