JP2000012016A - Negative electrode for battery and manufacturing method thereof - Google Patents
Negative electrode for battery and manufacturing method thereofInfo
- Publication number
- JP2000012016A JP2000012016A JP10174531A JP17453198A JP2000012016A JP 2000012016 A JP2000012016 A JP 2000012016A JP 10174531 A JP10174531 A JP 10174531A JP 17453198 A JP17453198 A JP 17453198A JP 2000012016 A JP2000012016 A JP 2000012016A
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- JP
- Japan
- Prior art keywords
- alloy
- negative electrode
- battery
- ball mill
- negative
- 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.)
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Classifications
-
- 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
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- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【0001】[0001]
【発明が属する技術分野】本発明は電池用負極活物質と
してMg合金を用いた負極およびその製造方法に関する
ものである。The present invention relates to a negative electrode using an Mg alloy as a negative electrode active material for a battery and a method for producing the same.
【0002】[0002]
【従来の技術】近年、ポータブル機器、コードレス機器
の発展に伴い、その電源である電池にはより一層の高エ
ネルギ−密度が要求される。この要求に対してLiイオ
ン電池やニッケル水素蓄電池が注目されている。さらな
る高エネルギー密度化に対しては、金属Liを負極に用
いた電池系が有力とされている。2. Description of the Related Art In recent years, with the development of portable devices and cordless devices, batteries as power sources thereof are required to have higher energy density. Li-ion batteries and nickel-metal hydride batteries have attracted attention in response to this demand. To further increase the energy density, a battery system using metal Li for the negative electrode is considered to be effective.
【0003】このように重量エネルギー密度の大きなL
iを負極に用いることによって高エネルギー密度の電池
が得られるが、Li資源は海水や岩塩水中に希釈に存在
しており、量産によってコスト面で安くなる目処がな
い。As described above, L having a large weight energy density
By using i for the negative electrode, a battery with a high energy density can be obtained, but Li resources are present in seawater or rock salt water in dilution, and there is no prospect that mass production will reduce the cost.
【0004】これに対して、Mgを負極に用いた電池系
では負極Mg1モルの反応で2電子が移動するため理論
的には金属Liを上回る高体積エネルギー密度の電池が
期待できる。さらに、資源的にも豊富で安価であり、環
境面でも有害でないため非常に期待の大きな負極材料で
ある。例えば、特開昭62−211861号公報、特開
平1−95469号公報あるいは特開平4−28172
号公報。On the other hand, in a battery system using Mg as the negative electrode, two electrons move by the reaction of 1 mole of the negative electrode Mg, so that a battery having a higher volume energy density than metal Li can be expected theoretically. Furthermore, since it is abundant and inexpensive in terms of resources and is not harmful in terms of the environment, it is a highly promising negative electrode material. For example, JP-A-62-121861, JP-A-1-95469 or JP-A-4-28172.
No. gazette.
【0005】[0005]
【発明が解決しようとする課題】しかし、この電池系で
は負極表面に絶縁物が形成され易く、電流が流れにくく
なる(過電圧が大きい)。そのため出力特性、容量、電
圧及びサイクル特性が悪くなる欠点があった。この対策
として、合金を細かく粉砕し、比表面積を増加させ、電
流密度を確保する方法が考えられる。しかし、通常のジ
ェットミル法や湿式の機械粉砕法では、作業中に表面に
強固な絶縁体である酸化被膜や水酸化物被膜が形成さ
れ、かえって出力特性が低下する課題があった。このた
め、従来は高エネルギー密度が期待されるMgの理論容
量のわずか10%〜20%程度の負極利用率に止まって
いた。However, in this battery system, an insulator is easily formed on the surface of the negative electrode, and current hardly flows (large overvoltage). For this reason, there is a disadvantage that the output characteristics, capacity, voltage and cycle characteristics are deteriorated. As a countermeasure, a method of pulverizing the alloy finely to increase the specific surface area and secure the current density can be considered. However, the conventional jet mill method or wet mechanical pulverization method has a problem in that an oxide film or a hydroxide film, which is a strong insulator, is formed on the surface during the operation, and the output characteristics are rather deteriorated. For this reason, in the past, the anode utilization rate was only about 10% to 20% of the theoretical capacity of Mg, which is expected to have a high energy density.
【0006】我々は鋭意検討を重ねた結果、高周波溶解
炉法あるいは不活性ガス中でのボールミル法や遊星ボー
ルミル法などのメカニカルアロイング法でMgにIn,
Ga,Tl,Cd,Mn,Coの少なくとも1種類を含
有したMg合金を作製することで合金表面の導電性を向
上し過電圧を下げ、負極の利用率を大きく増加させ、サ
イクル特性にも優れた電池を実現した。As a result of our intensive studies, we have found that Mg can be converted into In, Mg by mechanical alloying such as a high-frequency melting furnace method, a ball mill method in an inert gas, or a planetary ball mill method.
By producing an Mg alloy containing at least one of Ga, Tl, Cd, Mn, and Co, the conductivity of the alloy surface is improved, the overvoltage is reduced, the utilization rate of the negative electrode is greatly increased, and the cycle characteristics are also excellent. Battery realized.
【0007】[0007]
【課題を解決するための手段】以上の課題を解決するた
め本発明の電池用負極は、MgにIn,Ga,Tl,C
d,Mn,Co,Snの少なくとも1種類を含有したM
g合金が負極活物質であることを特徴とする。In order to solve the above problems, a negative electrode for a battery according to the present invention comprises In, Ga, Tl, C
M containing at least one of d, Mn, Co, and Sn
The g alloy is a negative electrode active material.
【0008】このとき、Mg合金中のMg量が70原子
%以上であることが有効である。また、Mg合金の表面
に、NiもしくはCuを付着したことが有効である。At this time, it is effective that the Mg content in the Mg alloy is 70 atomic% or more. It is effective that Ni or Cu is attached to the surface of the Mg alloy.
【0009】このとき、NiもしくはCuの付着量が1
0重量%以下であることが有効である。At this time, the amount of Ni or Cu attached is 1
It is effective that the content is 0% by weight or less.
【0010】以上の材料の製造方法は、高周波溶解法、
ボールミル法、遊星ボールミル法あるいは熱拡散法でM
g合金を作製することを特徴とする。[0010] The above-mentioned materials are produced by a high-frequency melting method,
Ball mill method, planetary ball mill method or heat diffusion method
It is characterized by producing a g alloy.
【0011】また、メカノフュージョン法もしくはメッ
キ法により、Mg合金の表面にNiもしくはCuを付着
したことを特徴とする。Further, Ni or Cu is adhered to the surface of the Mg alloy by a mechanofusion method or a plating method.
【0012】[0012]
【発明の実施の形態】本発明は負極活物質がMgにI
n,Ga,Tl,Cd,Mn,Co,Snの少なくとも
1種類を含有したMg合金からなることを特徴とする負
極である。BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, the negative electrode active material is made of Mg
A negative electrode comprising a Mg alloy containing at least one of n, Ga, Tl, Cd, Mn, Co, and Sn.
【0013】この際、Mg合金中のMg量は70原子%
以上であることが高エネルギー密度化のために望まし
い。さらに、Mg合金の表面にNiあるいはCuを10
重量%以下の量を付けることで電気化学特性の安定性が
増し、一層のサイクル特性の改善が図れる。この手段と
しては、メカノフュージョン法やハイブリダイゼーショ
ン法等の機械的な表面処理法あるいはメッキ法等の電気
化学的な方法がある。At this time, the Mg content in the Mg alloy is 70 atomic%.
It is desirable for the above to be higher for higher energy density. Further, Ni or Cu is added to the surface of the Mg alloy by 10%.
By adding the amount of not more than% by weight, the stability of the electrochemical characteristics is increased, and the cycle characteristics can be further improved. As this means, there are a mechanical surface treatment method such as a mechanofusion method and a hybridization method, and an electrochemical method such as a plating method.
【0014】また合金化の方法としては、高周波溶解法
あるいは不活性ガス中でのボールミル法、遊星ボールミ
ル法等のメカニカルアロイング(MA)法あるいは液体
金属にMgを浸漬後、熱拡散させる熱拡散法が有効であ
る。The alloying method may be a high frequency melting method, a mechanical milling (MA) method such as a ball mill method in an inert gas, a planetary ball mill method, or a thermal diffusion method in which Mg is immersed in a liquid metal and then thermally diffused. The law is valid.
【0015】Mgを負極に用いることで理論上はLiを
上回る体積エネルギー密度の電池が得られる。しかし、
実際にはMg表面に酸化被膜や水酸化物被膜が形成され
るため、分極(過電圧)が大きくなり、電池電圧が低く
なり電流密度も取れず、高いエネルギー密度が得られな
い。このため、比表面積を大きくすることが有効な手段
と考えられる。しかし、従来のジェットミルや湿式の機
械粉砕法ではMg表面に絶縁膜が形成され、過電圧が大
きくなる欠点があった。そこで、MgにIn,Ga,T
l,Cd,Mn,Co,Snの少なくとも1種類を含有
したMg合金を負極活物質に用いることで表面にできる
酸化膜や水酸化物被膜等が半導体化し過電圧が低下し電
池電圧、負極利用率及びサイクル特性が大幅に改善でき
ることがわかった。この際、Mg量としては70原子%
以上が高エネルギー密度化のために必要である。さら
に、Mg合金の表面にNiあるいはCuを付着させるこ
とで電気化学特性が安定し、サイクル特性の一層の向上
が図れた。By using Mg for the negative electrode, a battery having a volume energy density higher than that of Li in theory can be obtained. But,
Actually, since an oxide film or a hydroxide film is formed on the Mg surface, the polarization (overvoltage) increases, the battery voltage decreases, the current density cannot be obtained, and a high energy density cannot be obtained. Therefore, increasing the specific surface area is considered to be an effective means. However, the conventional jet mill or wet mechanical pulverization method has a drawback that an insulating film is formed on the Mg surface and the overvoltage is increased. Therefore, Mg, In, Ga, T
When an Mg alloy containing at least one of l, Cd, Mn, Co, and Sn is used as a negative electrode active material, an oxide film or a hydroxide film formed on the surface becomes a semiconductor, and the overvoltage is reduced. It was also found that the cycle characteristics could be greatly improved. At this time, the Mg content was 70 atomic%.
The above is necessary for higher energy density. Further, by attaching Ni or Cu to the surface of the Mg alloy, the electrochemical characteristics were stabilized, and the cycle characteristics were further improved.
【0016】合金化の方法としてはアーク溶解法や電子
ビーム溶解法や抵抗加熱法等では不均一に加熱されるた
め、Mgのような低沸点の金属では偏析が大きくなる傾
向がある。As an alloying method, since arc heating, electron beam melting, resistance heating, etc., heat non-uniformly, segregation tends to increase in low-boiling metals such as Mg.
【0017】以下に本発明の実施例を詳しく説明する。Hereinafter, embodiments of the present invention will be described in detail.
【0018】[0018]
【実施例】(実施例1)Mg80原子%とCo20原子
%を高周波真空溶解炉で溶解した後、水冷鋳型にこの溶
湯を流し込み急冷凝固させた。この様にしてMgCo合
金(バルク)を作製した後、アルゴンガス雰囲気でジョ
ー・クラシャー・ミルによって粗粉砕し、アルゴンガスに
よるジェットミルで平均粒径38μmまで微粉砕を行っ
た。Example 1 After melting 80 atomic% of Mg and 20 atomic% of Co in a high-frequency vacuum melting furnace, this molten metal was poured into a water-cooled mold and rapidly solidified. After preparing the MgCo alloy (bulk) in this way, it was coarsely pulverized by a Joe Crusher mill in an argon gas atmosphere, and finely pulverized by an argon gas jet mill to an average particle size of 38 μm.
【0019】次に、このMgCo合金粉末100重量部
にジメチルアセトアミド(DMAA)と0.6molのMg
(ClO4)2からなる電解液を少量添加し、ポリテトラフ
ルオロエチレン(PTFE)粉末を3重量部結着剤とし
て添加し負極ペーストとした。この負極ペーストを、M
o製のパンチングメタル芯材に塗着、プレスした後、真
空中180℃30分間加熱してPTFEを融解し、負極
を作製した。電解液には、DMAAと0.5molのMg
(ClO4)2からなる非水系電解質を、正極には負極容量
より十分大容量の電解二酸化マンガン(MnO2)を用
い、2極式試験セルで負極規制の液リッチ電池を作製し
た。Next, dimethylacetamide (DMAA) and 0.6 mol of Mg were added to 100 parts by weight of the MgCo alloy powder.
A small amount of an electrolyte solution of (ClO 4 ) 2 was added, and 3 parts by weight of polytetrafluoroethylene (PTFE) powder was added as a binder to prepare a negative electrode paste. This negative electrode paste is
After being applied to a perforated metal core material made of o and pressed, it was heated in a vacuum at 180 ° C. for 30 minutes to melt PTFE, thereby producing a negative electrode. The electrolyte solution includes DMAA and 0.5 mol of Mg.
A non-aqueous electrolyte composed of (ClO 4 ) 2 and electrolytic manganese dioxide (MnO 2 ) having a capacity sufficiently larger than the capacity of the negative electrode were used for the positive electrode, and a negative electrode-regulated liquid-rich battery was produced using a bipolar test cell.
【0020】次に充放電試験を充電電流2mA/gで120
%充電、放電は2mA/g、1.1Vカットの条件で行っ
た。比較例1として実施例1と同様に鋳造法でMgのみ
のバルクを作製し、機械粉砕で平均粒径40μmのMg
微粒子を作製し、実施例と同様の方法で負極を作製し、
電池を構成した。Next, a charge / discharge test was conducted at a charge current of 2 mA / g for 120 minutes.
% Charge and discharge were performed under the conditions of 2 mA / g and 1.1 V cut. As Comparative Example 1, a bulk containing only Mg was produced by a casting method in the same manner as in Example 1, and Mg having an average particle size of 40 μm was obtained by mechanical pulverization.
Fine particles were prepared, a negative electrode was prepared in the same manner as in the example,
A battery was configured.
【0021】また、製造方法の比較のためMgとCoの
仕込み比を本実施例と同じとし、アーク溶解炉、電子ビ
ーム溶解及び抵抗加熱法で作製した合金を用いて、本実
施例と同様の方法で粉砕、負極作製、電池構成、特性評
価を行った(比較例2〜4)。For comparison of the manufacturing method, the charging ratio of Mg and Co was set to be the same as that of the present embodiment, and an alloy prepared by an arc melting furnace, electron beam melting and resistance heating was used. Pulverization, production of a negative electrode, battery configuration, and characteristic evaluation were performed by the method (Comparative Examples 2 to 4).
【0022】表1に平均放電電圧及び負極利用率(実容
量/理論容量)及び容量維持率(50サイクル容量/初
期容量)の比較を示した。Table 1 shows a comparison between the average discharge voltage, the negative electrode utilization rate (actual capacity / theoretical capacity), and the capacity retention rate (50 cycle capacity / initial capacity).
【0023】表1からわかるように本実施例の電池は従
来のMg(比較例1)や他の製造方法(比較例2〜4)
に比べ平均放電電圧が高く、負極利用率も大きく向上し
た。これはMg負極では表面に強固な酸化被膜や水酸化
被膜が形成され、過電圧が大きくなるためと考えられ
る。一方、アーク溶解法や電子ビーム溶解法や抵抗加熱
法ではMgだけが初期に溶けCoが偏析することがわか
った。これによってMg単体の性質が強く現れたものと
考えられる。As can be seen from Table 1, the battery according to the present embodiment uses the conventional Mg (Comparative Example 1) and other manufacturing methods (Comparative Examples 2 to 4).
, The average discharge voltage was higher and the utilization rate of the negative electrode was greatly improved. This is considered to be because a strong oxide film or a hydroxide film is formed on the surface of the Mg negative electrode, and the overvoltage increases. On the other hand, it was found that in the arc melting method, the electron beam melting method and the resistance heating method, only Mg was initially melted and Co segregated. It is considered that the properties of Mg alone appeared strongly.
【0024】[0024]
【表1】 [Table 1]
【0025】(実施例2)Mg(100メッシュ以下)と
Mn(100メッシュ以下)を70原子%と30原子%の
比率で総量20gを1Lのステンレス製のボールミルポ
ットに投入し、10日間ボールミルを行った。回収した
MgMn合金微粒子は平均粒径が30μmであった。こ
のMgMn合金粉末を用いて実施例1と同様の方法、構
成で非水系電解質の負極規制液リッチ電池を作製した。Example 2 A total of 20 g of Mg (100 mesh or less) and Mn (100 mesh or less) in a ratio of 70 atom% and 30 atom% was put into a 1 L stainless steel ball mill pot. went. The recovered MgMn alloy fine particles had an average particle size of 30 μm. Using this MgMn alloy powder, a nonaqueous electrolyte negative electrode regulating liquid-rich battery was produced in the same manner and in the same manner as in Example 1.
【0026】次に充放電試験を充電電流2mA/gで120
%充電、放電は2mA/g、1.1Vカットの条件で行っ
た。表1に平均放電電圧、負極利用率及び容量維持率を
示す。比較のためにMnの代わりにFe、Al、Si、
Cr、Cu、Tiを各々30at%添加したものを作製
し、本実施例と同様の方法で電池を構成し、特性を評価
した(比較例5〜10)。Next, a charge / discharge test was conducted at a charge current of 2 mA / g for 120 minutes.
% Charge and discharge were performed under the conditions of 2 mA / g and 1.1 V cut. Table 1 shows the average discharge voltage, the negative electrode utilization rate, and the capacity retention rate. For comparison, instead of Mn, Fe, Al, Si,
A battery in which Cr, Cu, and Ti were added at 30 at% each was produced, and a battery was constructed in the same manner as in this example, and the characteristics were evaluated (Comparative Examples 5 to 10).
【0027】表1から本実施例の電池は平均放電電圧、
負極利用率が高く、容量維持率も大きいことがわかっ
た。一方、Feを始めとする他の組成からなるMg合金
では平均放電電圧、負極利用率が低く、合金化による特
性向上効果は認められなかった。また、Mnの添加量と
しては30原子%を越すとMg量が減少するため放電容
量自体が顕著に低下した。この傾向はMn以外のCo、
In、Ga、Tl、Cd、Snでも認められた。From Table 1, it can be seen that the battery of this embodiment has an average discharge voltage,
It was found that the negative electrode utilization rate was high and the capacity retention rate was also high. On the other hand, the average discharge voltage and the negative electrode utilization rate were low in the Mg alloy having another composition such as Fe, and the effect of improving the characteristics by alloying was not recognized. Further, when the amount of Mn added exceeds 30 atomic%, the amount of Mg is reduced, so that the discharge capacity itself is significantly reduced. This tendency is due to Co other than Mn,
In, Ga, Tl, Cd and Sn were also observed.
【0028】(実施例3)Mg板(2cm×4cm×0.
5mm)をアルゴン雰囲気におかれた80℃のGa浴中
に8時間浸漬した後、Mg板を取り出しアルゴン中で4
00℃10時間の熱処理を行った。断面のEPMA(電
子線マイクロ分析)による組成分析の結果、ほぼ均一に
GaがMg板内部まで拡散していることがわかった。G
a量としては約8at%であった。このMgGa合金板に
Niリードをスポット溶接で取り付け、負極とした。実
施例1と同様の電池構成で非水系電解質の負極規制液リ
ッチ電池を作製した。Example 3 Mg plate (2 cm × 4 cm × 0.2 mm)
5 mm) was immersed in a Ga bath at 80 ° C. in an argon atmosphere for 8 hours.
Heat treatment was performed at 00 ° C. for 10 hours. As a result of composition analysis of the cross section by EPMA (electron beam micro analysis), it was found that Ga was diffused almost uniformly to the inside of the Mg plate. G
The amount of a was about 8 at%. A Ni lead was attached to this MgGa alloy plate by spot welding to form a negative electrode. With the same battery configuration as in Example 1, a non-aqueous electrolyte negative electrode regulation liquid-rich battery was produced.
【0029】次に充放電試験を充電電流2mA/gで120
%充電、放電は2mA/g、1.1Vカットの条件で行っ
た。比較のためMg板を負極に用いた電池を同様の製造
条件で作製した(比較例11)。Next, a charge / discharge test was performed at a charge current of 2 mA / g for 120 minutes.
% Charge and discharge were performed under the conditions of 2 mA / g and 1.1 V cut. For comparison, a battery using an Mg plate as the negative electrode was manufactured under the same manufacturing conditions (Comparative Example 11).
【0030】表1に平均放電電圧、負極利用率及び容量
維持率を示した。実施例1や実施例2のような粉砕品に
比べて負極利用率は低下したが、比較例11に比べて、
大幅な特性の向上が認められた。Table 1 shows the average discharge voltage, the negative electrode utilization rate and the capacity retention rate. Although the negative electrode utilization rate was lower than that of the pulverized products such as Example 1 and Example 2, compared to Comparative Example 11,
Significant improvement in properties was observed.
【0031】(実施例4)実施例3においてGaの代わ
りにInを用いた。アルゴン雰囲気におかれた200℃
のIn浴中に8時間浸漬した後、Mg板を取り出しアル
ゴン中で500℃10時間の熱処理を行った。断面のE
PMAによる組成分析の結果、ほぼ均一にInがMg板
内部まで拡散していることがわかった。In量としては
約6at%であった。実施例3と同様の構成、条件で負極
規制液リッチ電池を作製した。Example 4 In Example 3, In was used instead of Ga. 200 ° C in an argon atmosphere
After immersion in an In bath for 8 hours, the Mg plate was taken out and heat-treated at 500 ° C. for 10 hours in argon. Section E
As a result of composition analysis by PMA, it was found that In was diffused almost uniformly to the inside of the Mg plate. The amount of In was about 6 at%. A negative electrode regulated liquid rich battery was manufactured under the same configuration and conditions as in Example 3.
【0032】表1に各種電池特性を示すが、Mg板負極
よりも高電圧、高負極利用率、高容量維持率となった。Table 1 shows the characteristics of various batteries. The results are higher voltage, higher negative electrode utilization rate, and higher capacity retention rate than the Mg plate negative electrode.
【0033】(実施例5)Mg(100メッシュ以下)と
Cd(100メッシュ以下)とを90at%と10at%の比
率で総量10gを500ccのステンレス製の遊星ボール
ミル用ポットに投入し、その中に直径20mmのステン
レスボールを20個、直径10mmのステンレスボール
を40個挿入した。ポット内をアルゴン置換した後、回
転数2000rpmで3日間遊星ボールミルを行った。
回収したMgCd合金微粒子は平均粒径が25μmであ
った。このMgCd合金粉末を用いて実施例1と同様の
方法、構成で非水系電解質の負極規制液リッチ電池を作
製した。Example 5 Mg (100 mesh or less) and Cd (100 mesh or less) were put into a 500 cc stainless steel ball mill pot at a ratio of 90 at% and 10 at% in a total amount of 10 g. Twenty 20 stainless steel balls having a diameter of 20 mm and 40 stainless steel balls having a diameter of 10 mm were inserted. After the inside of the pot was purged with argon, a planetary ball mill was performed at a rotation speed of 2000 rpm for 3 days.
The recovered MgCd alloy fine particles had an average particle size of 25 μm. Using this MgCd alloy powder, a non-aqueous electrolyte negative electrode regulating liquid-rich battery was produced in the same manner and in the same manner as in Example 1.
【0034】次に実施例1と同様に充電電流2mA/gで1
20%充電、放電は2mA/g、1.1Vカットの条件で充
放電試験を行った。Next, in the same manner as in the first embodiment, 1
A charge / discharge test was performed under conditions of 20% charge and discharge at 2 mA / g and 1.1 V cut.
【0035】表1に各種電池特性を示したが、本実施例
の電池は放電電圧、負極利用率および容量維持率のすべ
ての点で優れることがわかった。Table 1 shows various battery characteristics, and it was found that the battery of this example was excellent in all aspects of the discharge voltage, the negative electrode utilization rate, and the capacity retention rate.
【0036】(実施例6および7)実施例1と同様の高
周波溶解法でMgTl合金(Tl5原子%)を作製後、
機械粉砕で平均粒径が32μmのMgTI合金粉末を作
製した。(Examples 6 and 7) An MgTl alloy (Tl5 at%) was prepared by the same high-frequency melting method as in Example 1,
An MgTI alloy powder having an average particle size of 32 μm was produced by mechanical pulverization.
【0037】次に、この合金粒子15gに、粒径30n
mのNi微粒子1.3g(8重量%)をアルゴン中でメ
カノフュージョン処理(ホソカワミクロン製AM−15
F使用、ギャップ1mm、1200rpm、15分間)
し、MgTl合金粒子表面にNiの微粉末を均一に付着
させた。Next, 15 g of the alloy particles were added with a particle size of 30 n.
1.3 g (8% by weight) of Ni fine particles having a m of 1.5 m were mechanofusion treated with argon (AM-15 manufactured by Hosokawa Micron).
F use, gap 1mm, 1200rpm, 15 minutes)
Then, fine Ni powder was uniformly attached to the surfaces of the MgTl alloy particles.
【0038】MgTl合金粉末(実施例5)及びNi付
着複合粒子(実施例6)を用いて実施例1と同様の方
法、構成で非水系電解質の負極規制液リッチ電池を作製
した。Using the MgTl alloy powder (Example 5) and the Ni-adhered composite particles (Example 6), a nonaqueous electrolyte negative electrode regulating liquid-rich battery was produced in the same manner and in the same manner as in Example 1.
【0039】次に実施例1と同様に充放電試験を充電電
流2mA/gで120%充電、放電は2mA/g、1.1Vカッ
トの条件で行った。表1からNiを合金表面に付着させ
ることで電池のサイクル特性(容量維持率)が向上する
ことがわかった。Next, in the same manner as in Example 1, a charge / discharge test was performed at a charge current of 2 mA / g at 120%, and discharge was performed at 2 mA / g and 1.1 V cut. From Table 1, it was found that the cycle characteristics (capacity maintenance rate) of the battery were improved by attaching Ni to the alloy surface.
【0040】(実施例8および9)Mg(75原子
%)、Sn(25原子%)より高周波真空溶解炉で溶解
した後、ロール急冷法によってMgSn合金箔を作製し
た。次に、この合金箔(5mm×5cm×0.2mm)
にリード線を取り付け、これを陰極とし、メッキ浴とし
て硫酸銅水溶液、陽極にCu板を用いて合金箔表面にC
uを電解メッキ(4重量%)した。水洗・乾燥後、この
合金箔を負極として実施例1と同様の構成の非水系電解
質の負極規制液リッチ電池(実施例9)を作製した。メ
ッキ前の合金箔を負極とした電池も同様に作製した(実
施例8)。(Examples 8 and 9) Mg (75 at%) and Sn (25 at%) were melted in a high-frequency vacuum melting furnace, and then MgSn alloy foil was produced by a roll quenching method. Next, this alloy foil (5 mm x 5 cm x 0.2 mm)
A lead wire is attached to the cathode, this is used as a cathode, an aqueous solution of copper sulfate is used as a plating bath, and a Cu plate is used as an anode.
u was electrolytically plated (4% by weight). After washing with water and drying, a nonaqueous electrolyte negative electrode regulating liquid-rich battery (Example 9) having the same structure as in Example 1 was produced using this alloy foil as the negative electrode. A battery using the alloy foil before plating as a negative electrode was similarly manufactured (Example 8).
【0041】次に実施例1と同様に充放電試験を充電電
流2mA/gで120%充電、放電は2mA/g、1.1Vカッ
トの条件で行った。MgSn合金箔の電池は放電電圧、
負極利用率および容量維持率のすべての点でMg板の電
池(比較例11)より優れることがわかった。Cuメッ
キしたものは放電電圧及び負極利用率が若干低下したが
容量維持率は大きく向上することがわかった。Next, in the same manner as in Example 1, a charge / discharge test was performed at a charge current of 2 mA / g at 120%, and discharge was performed at 2 mA / g and 1.1 V cut. MgSn alloy foil batteries have discharge voltage,
It was found that the negative electrode utilization rate and the capacity retention rate were all superior to the Mg plate battery (Comparative Example 11). It was found that the discharge voltage and the utilization rate of the negative electrode slightly decreased in the case of Cu plating, but the capacity retention rate was greatly improved.
【0042】[0042]
【発明の効果】上記実施例から明らかなように、本発明
の電池及びその製造方法は負極としてIn,Ga,T
l,Cd,Mn,Co,Snの少なくとも1種類を含有
したMg合金を用いることで表面に半導体が形成され抵
抗成分が減少するため、過電圧が大幅に低下しレート特
性、負極利用率が向上し、Mgの持つ高エネルギー密度
を引き出すことができる。さらに、Mg合金の表面にN
i層やCu層を設けることで電気化学特性が安定化し、
サイクル特性が向上し長寿命となる。但し、Mg量とし
ては容量の点から70原子%以上は必要である。As is apparent from the above examples, the battery of the present invention and the method for producing the same are characterized in that In, Ga, T
By using a Mg alloy containing at least one of l, Cd, Mn, Co, and Sn, a semiconductor is formed on the surface and the resistance component is reduced. Therefore, the overvoltage is significantly reduced, and the rate characteristics and the anode utilization rate are improved. And the high energy density of Mg. In addition, N
By providing an i layer and a Cu layer, the electrochemical characteristics are stabilized,
The cycle characteristics are improved and the life is extended. However, the amount of Mg must be 70 atomic% or more from the viewpoint of capacity.
【0043】合金の製造方法としては高周波溶解法、ボ
ールミル法、遊星ボールミル法などのメカニカルアロイ
ング法あるいは熱拡散法が有効である。特に、メカニカ
ルアロイング法は融点の大きく異なる異種金属の合金化
や沸点の低い金属の合金化に対して非常に有効な手段で
ある。As a method for producing the alloy, a mechanical alloying method such as a high-frequency melting method, a ball mill method, and a planetary ball mill method or a heat diffusion method is effective. In particular, the mechanical alloying method is a very effective means for alloying dissimilar metals having greatly different melting points or alloying metals having low boiling points.
【0044】さらに、Mg合金表面にNiやCuを処理
する手段としては、合金組成にメカノフュージョン法等
の機械的表面処理あるいはメッキ法等の電気化学処理が
ある。Further, as a means for treating Ni or Cu on the surface of the Mg alloy, there is a mechanical surface treatment such as a mechanofusion method or an electrochemical treatment such as a plating method for the alloy composition.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) H01M 10/40 H01M 10/40 Z (72)発明者 伊藤 修二 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 4K018 BA07 BC16 BC20 BC22 KA38 5H003 AA01 AA02 AA04 BA00 BA01 BA07 BB00 BB02 BC01 BC05 BD04 5H014 AA02 BB01 BB08 BB12 EE05 HH01 5H029 AJ03 AJ05 AK02 AL11 AM01 AM02 AM07 CJ02 CJ08 CJ22 CJ24 DJ16 HJ01 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) H01M 10/40 H01M 10/40 Z (72) Inventor Shuji Ito 1006 Kazuma, Kadoma, Osaka Prefecture Matsushita Electric Industrial In-house F term (reference) 4K018 BA07 BC16 BC20 BC22 KA38 5H003 AA01 AA02 AA04 BA00 BA01 BA07 BB00 BB02 BC01 BC05 BD04 5H014 AA02 BB01 BB08 BB12 EE05 HH01 5H029 AJ03 AJ05 AK02 AL11 AM01 AM02 C07 C02
Claims (6)
Co,Snの少なくとも1種類を含有したMg合金が負
極活物質であることを特徴とする電池用負極。1. The method according to claim 1, wherein Mg is In, Ga, Tl, Cd, Mn,
A negative electrode for a battery, wherein a Mg alloy containing at least one of Co and Sn is a negative electrode active material.
あることを特徴とする請求項1記載の電池用負極。2. The negative electrode for a battery according to claim 1, wherein the amount of Mg in the Mg alloy is 70 atomic% or more.
付着したことを特徴とする請求項1または2記載の電池
用負極。3. The battery negative electrode according to claim 1, wherein Ni or Cu is attached to the surface of the Mg alloy.
以下であることを特徴とする請求項3記載の電池用負
極。4. An adhesion amount of Ni or Cu is 10% by weight.
The negative electrode for a battery according to claim 3, wherein:
ルミル法あるいは熱拡散法でMg合金を作製することを
特徴とする請求項1、2、3または4記載の電池用負極
の製造方法。5. The method for producing a negative electrode for a battery according to claim 1, wherein the Mg alloy is produced by a high frequency melting method, a ball mill method, a planetary ball mill method or a thermal diffusion method.
により、Mg合金の表面にNiもしくはCuを付着した
ことを特徴とする請求項3または4記載の電池用負極の
製造方法。6. The method for producing a negative electrode for a battery according to claim 3, wherein Ni or Cu is adhered to the surface of the Mg alloy by a mechanofusion method or a plating method.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10174531A JP2000012016A (en) | 1998-06-22 | 1998-06-22 | Negative electrode for battery and manufacturing method thereof |
| US09/323,892 US6265109B1 (en) | 1998-06-02 | 1999-06-02 | Magnesium alloy battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10174531A JP2000012016A (en) | 1998-06-22 | 1998-06-22 | Negative electrode for battery and manufacturing method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000012016A true JP2000012016A (en) | 2000-01-14 |
Family
ID=15980167
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10174531A Pending JP2000012016A (en) | 1998-06-02 | 1998-06-22 | Negative electrode for battery and manufacturing method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000012016A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1315213C (en) * | 2003-06-17 | 2007-05-09 | 李华伦 | Magnesium manganese laminated battery pack |
| US8361651B2 (en) | 2011-04-29 | 2013-01-29 | Toyota Motor Engineering & Manufacturing North America, Inc. | Active material for rechargeable battery |
| JP2013191481A (en) * | 2012-03-15 | 2013-09-26 | Furukawa Battery Co Ltd:The | Metal electrode, manufacturing method therefor, and magnesium cell |
| US8685564B2 (en) | 2011-06-22 | 2014-04-01 | Toyota Motor Engineering & Manufacturing North America, Inc. | Active material for rechargeable battery |
| JP2014167933A (en) * | 2011-04-18 | 2014-09-11 | Tohoku Univ | Negative electrode material for magnesium cell and magnesium cell |
| JP2015015153A (en) * | 2013-07-04 | 2015-01-22 | 積水化学工業株式会社 | Electrode material, magnesium fuel battery, and method for manufacturing electrode material |
| JP2015515728A (en) * | 2012-04-05 | 2015-05-28 | トヨタ モーター エンジニアリング アンド マニュファクチャリング ノース アメリカ,インコーポレイテッド | Rechargeable magnesium battery active material |
| US10615452B2 (en) | 2011-06-22 | 2020-04-07 | Toyota Motor Engineering & Manufacturing North America, Inc. | High voltage rechargeable magnesium cell |
| CN111916766A (en) * | 2020-06-24 | 2020-11-10 | 太原理工大学 | Mg-Bi-Ca-In alloy as negative electrode material of magnesium air battery and preparation method thereof |
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| JP2023530973A (en) * | 2020-07-15 | 2023-07-20 | シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲー | Anode for magnesium battery and method of making same |
-
1998
- 1998-06-22 JP JP10174531A patent/JP2000012016A/en active Pending
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|---|---|---|---|---|
| CN1315213C (en) * | 2003-06-17 | 2007-05-09 | 李华伦 | Magnesium manganese laminated battery pack |
| JP2014167933A (en) * | 2011-04-18 | 2014-09-11 | Tohoku Univ | Negative electrode material for magnesium cell and magnesium cell |
| US8361651B2 (en) | 2011-04-29 | 2013-01-29 | Toyota Motor Engineering & Manufacturing North America, Inc. | Active material for rechargeable battery |
| US8685564B2 (en) | 2011-06-22 | 2014-04-01 | Toyota Motor Engineering & Manufacturing North America, Inc. | Active material for rechargeable battery |
| US10615452B2 (en) | 2011-06-22 | 2020-04-07 | Toyota Motor Engineering & Manufacturing North America, Inc. | High voltage rechargeable magnesium cell |
| JP2013191481A (en) * | 2012-03-15 | 2013-09-26 | Furukawa Battery Co Ltd:The | Metal electrode, manufacturing method therefor, and magnesium cell |
| JP2015515728A (en) * | 2012-04-05 | 2015-05-28 | トヨタ モーター エンジニアリング アンド マニュファクチャリング ノース アメリカ,インコーポレイテッド | Rechargeable magnesium battery active material |
| JP2015015153A (en) * | 2013-07-04 | 2015-01-22 | 積水化学工業株式会社 | Electrode material, magnesium fuel battery, and method for manufacturing electrode material |
| CN111916766A (en) * | 2020-06-24 | 2020-11-10 | 太原理工大学 | Mg-Bi-Ca-In alloy as negative electrode material of magnesium air battery and preparation method thereof |
| CN111916766B (en) * | 2020-06-24 | 2022-09-02 | 太原理工大学 | Mg-Bi-Ca-In alloy as negative electrode material of magnesium air battery and preparation method thereof |
| JP2023530973A (en) * | 2020-07-15 | 2023-07-20 | シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲー | Anode for magnesium battery and method of making same |
| JP7566935B2 (en) | 2020-07-15 | 2024-10-15 | シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲー | Anode for magnesium battery and method of making same |
| CN114045406A (en) * | 2021-10-25 | 2022-02-15 | 河海大学 | A kind of magnesium alloy negative electrode plate for seawater battery and preparation method thereof |
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