JPH0782838B2 - Rechargeable negative electrode for electrochemical device - Google Patents
Rechargeable negative electrode for electrochemical deviceInfo
- Publication number
- JPH0782838B2 JPH0782838B2 JP59107804A JP10780484A JPH0782838B2 JP H0782838 B2 JPH0782838 B2 JP H0782838B2 JP 59107804 A JP59107804 A JP 59107804A JP 10780484 A JP10780484 A JP 10780484A JP H0782838 B2 JPH0782838 B2 JP H0782838B2
- Authority
- JP
- Japan
- Prior art keywords
- alloy
- negative electrode
- discharge
- amount
- charge
- 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
- 229910045601 alloy Inorganic materials 0.000 claims description 50
- 239000000956 alloy Substances 0.000 claims description 50
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 claims description 19
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 17
- 229910052793 cadmium Inorganic materials 0.000 claims description 17
- 239000011255 nonaqueous electrolyte Substances 0.000 claims description 14
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 8
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 8
- 229910052787 antimony Inorganic materials 0.000 claims description 8
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 8
- 229910052791 calcium Inorganic materials 0.000 claims description 8
- 239000011575 calcium Substances 0.000 claims description 8
- 229910052738 indium Inorganic materials 0.000 claims description 8
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 claims description 8
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims description 8
- 229910052753 mercury Inorganic materials 0.000 claims description 8
- 229910052709 silver Inorganic materials 0.000 claims description 8
- 239000004332 silver Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 7
- 239000003792 electrolyte Substances 0.000 claims description 7
- 229910001413 alkali metal ion Inorganic materials 0.000 claims description 4
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 150000001340 alkali metals Chemical class 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 40
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 18
- 229910052744 lithium Inorganic materials 0.000 description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 15
- 230000001186 cumulative effect Effects 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 8
- 239000002904 solvent Substances 0.000 description 7
- 229910000925 Cd alloy Inorganic materials 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 6
- 229910052797 bismuth Inorganic materials 0.000 description 6
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 210000004027 cell Anatomy 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 3
- 229910001416 lithium ion Inorganic materials 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 229910000978 Pb alloy Inorganic materials 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 210000001787 dendrite Anatomy 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- MHCFAGZWMAWTNR-UHFFFAOYSA-M lithium perchlorate Chemical compound [Li+].[O-]Cl(=O)(=O)=O MHCFAGZWMAWTNR-UHFFFAOYSA-M 0.000 description 2
- 229910001486 lithium perchlorate Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 description 1
- 229910000733 Li alloy Inorganic materials 0.000 description 1
- 229910013063 LiBF 4 Inorganic materials 0.000 description 1
- CSBHIHQQSASAFO-UHFFFAOYSA-N [Cd].[Sn] Chemical compound [Cd].[Sn] CSBHIHQQSASAFO-UHFFFAOYSA-N 0.000 description 1
- YVTIXMVVDLCGIJ-UHFFFAOYSA-N [Cd].[Sn].[Pb] Chemical compound [Cd].[Sn].[Pb] YVTIXMVVDLCGIJ-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000002788 crimping Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000001989 lithium alloy Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 229910002058 ternary alloy Inorganic materials 0.000 description 1
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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
-
- 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
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/40—Alloys based on alkali metals
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (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、ポータブル電源やメモリーバックアップ電源
として使用する二次電池やキャパシターなどの再充電可
能な電気化学装置の負極に関するものである。TECHNICAL FIELD The present invention relates to a negative electrode of a rechargeable electrochemical device such as a secondary battery or a capacitor used as a portable power supply or a memory backup power supply.
従来例の構成とその問題点 リチウムなどのアルカリ金属を負極とする非水電解質二
次電池の開発が進められている。金属リチウムを負極と
する非水電解質二次電池では、充電時に負極のリチウム
上にデンドライトが発生し、正極との間で短絡したり、
あるいはリチウムが小球状に析出して負極から脱離する
などして、充放電効率の低下、サイクル特性の低下の原
因となっていた。Configuration of Conventional Example and Problems Thereof A non-aqueous electrolyte secondary battery using an alkali metal such as lithium as a negative electrode is under development. In a non-aqueous electrolyte secondary battery using metal lithium as a negative electrode, dendrite is generated on the lithium of the negative electrode during charging, short-circuiting with the positive electrode,
Alternatively, lithium is deposited in the form of small spheres and desorbs from the negative electrode, which causes a decrease in charge / discharge efficiency and a decrease in cycle characteristics.
この問題を克服するために、スズや鉛とカドミウムの合
金を負極に使用することが提案されている。例えば、鉛
とカドミウムの合金を負極に使用すると、充電時に、非
水電解質中のリチウムイオンが負極の鉛−カドミウム合
金に吸蔵されてリチウムとの合金を作り、放電時には、
吸蔵されたリチウムが非水電解質中にリチウムイオンと
して放出される。このように、リチウムのデンドライト
の発生もなく、またリチウムが小球状となって負極から
脱離することもなく、充放電効率の高い、サイクル特性
の良い負極となる。また負極の合金中にカドミウムを含
ませることになり、リチウムを吸蔵する際にも、負極の
粉末化が起こらないなど優れた負極となる。In order to overcome this problem, it has been proposed to use tin or an alloy of lead and cadmium for the negative electrode. For example, when an alloy of lead and cadmium is used for the negative electrode, during charging, lithium ions in the non-aqueous electrolyte are occluded by the negative electrode lead-cadmium alloy to form an alloy with lithium, and during discharge,
The stored lithium is released as lithium ions into the non-aqueous electrolyte. As described above, the dendrite of lithium is not generated, and the lithium does not become a small spherical shape and is desorbed from the negative electrode, and the negative electrode has high charge / discharge efficiency and excellent cycle characteristics. In addition, since cadmium is included in the alloy of the negative electrode, it becomes an excellent negative electrode in which powdering of the negative electrode does not occur even when occluding lithium.
ここで、サイクル特性や、低率充放電時の充放電量、つ
まり、単位体積当りまたは重量当り、より大きい充放電
量が得られる条件下での検討の結果より、スズや鉛の含
量が45重量%以上の合金が良いとされて来た。これは、
合金中のスズや鉛が、充放電に伴うリチウムの吸蔵,放
出にかかわり、カドミウムは、負極の粉末化を防ぐ結着
剤の役割を果たしているからである。Here, based on the cycle characteristics and the charge / discharge amount at low rate charge / discharge, that is, the result of the examination under the condition that a larger charge / discharge amount per unit volume or weight is obtained, the content of tin or lead is 45% or less. It has been said that alloys with a weight percentage or more are good. this is,
This is because tin and lead in the alloy are involved in the storage and release of lithium during charge and discharge, and cadmium plays the role of a binder that prevents pulverization of the negative electrode.
しかし、この合金を用いた場合にも、充放電中にガスが
発生するという問題があった。この発生ガスのため、密
閉した電池では、電池ケースのふくれが生じたり、ある
いは負極と正極の間にたまって充放電特性の低下をまね
いたりする。発生ガスを分析すると、大部分が酸素や窒
素といった空気の成分であるが、ごく少量ではあるが、
非水電解質の溶媒に用いているプロピレンカーボネート
の分解生成物であると推定されるプロピレンがある。However, even when this alloy is used, there is a problem that gas is generated during charging and discharging. Due to this generated gas, in a sealed battery, the battery case may swell, or it may accumulate between the negative electrode and the positive electrode, leading to deterioration of charge / discharge characteristics. When the generated gas is analyzed, most of it is air components such as oxygen and nitrogen, but only a small amount,
There is propylene which is presumed to be a decomposition product of propylene carbonate used as a solvent for the non-aqueous electrolyte.
このガス発生の課題に対しては、負極に使用する合金を
溶融状態で真空にして合金中から酸素や窒素を除く方
法、あるいは充電により合金中にリチウムを吸蔵させた
後真空に脱気して取り除く方法がある。この方法により
負極からのガス発生の大部分である酸素や窒素の発生は
防ぐことができ、密閉電池においてもサイクル特性は向
上する。しかし、非水電解質の溶媒を分解して発生する
ガスについて、まだ問題が残っている。To solve this gas generation problem, the alloy used for the negative electrode should be vacuumed in the molten state to remove oxygen and nitrogen from the alloy, or lithium should be stored in the alloy by charging and then degassed to vacuum. There is a way to get rid of it. By this method, most of the gas generated from the negative electrode can be prevented from being generated, such as oxygen and nitrogen, and the cycle characteristics are improved even in the sealed battery. However, there still remains a problem regarding the gas generated by decomposing the solvent of the non-aqueous electrolyte.
特に、正極に活性炭を用い、負極に前記の合金を用いる
再充電可能な電気化学装置は、充放電容量は、活性炭の
容量が小さいために小であるが、充放電サイクル特性
は、数千サイクル以上が要求される。このようなサイク
ル特性を満足するには、負極において非水電解質の溶媒
の分解によるガス発生も防止する必要がある。In particular, a rechargeable electrochemical device that uses activated carbon for the positive electrode and the above alloy for the negative electrode has a small charge / discharge capacity because the activated carbon has a small capacity, but the charge / discharge cycle characteristics are several thousand cycles. The above is required. In order to satisfy such cycle characteristics, it is necessary to prevent gas generation due to decomposition of the solvent of the non-aqueous electrolyte in the negative electrode.
発明の目的 本発明の目的は、再充電可能な電気化学装置の負極とし
て、充放電をくり返しても、使用している非水電解質の
分解によるガス発生を少なくすることのできる合金を提
供することであり、これよりサイクル特性の優れた電気
化学装置を得ることが可能となる。OBJECT OF THE INVENTION It is an object of the present invention to provide an alloy which can reduce gas generation due to decomposition of a non-aqueous electrolyte used as a negative electrode of a rechargeable electrochemical device even when charging and discharging are repeated. Therefore, it becomes possible to obtain an electrochemical device having excellent cycle characteristics.
発明の構成 本発明の負極は、充放電の可逆性を有する正極及びアル
カリ金属イオンを含む非水電解質と組み合わせて再充電
可能な電気化学装置を構成するもので、充電により非水
電解質中のアルカリ金属イオンを吸蔵してアルカリ金属
との合金を作り、放電によりアルカリ金属イオンとして
非水電解質中に放出する合金からなり、この合金がス
ズ,鉛の群から選ばれた少くとも1種の10重量%以上45
重量%未満とカドミウムからなる。さらにこの合金が、
ビスマス,インジウム,カルシウム,アンチモン,水
銀,銀の群から選ばれた少なくとも1種を20重量%以下
の範囲で含んでいてもよい。これらの合金を用いること
により、充放電をくり返しても、電解質の分解によるガ
ス発生を少なくすることができる。The negative electrode of the present invention constitutes a rechargeable electrochemical device in combination with a positive electrode having charge-discharge reversibility and a non-aqueous electrolyte containing an alkali metal ion. It consists of an alloy that occludes metal ions to form an alloy with an alkali metal and discharges it into the non-aqueous electrolyte as an alkali metal ion upon discharge. This alloy is at least 10% by weight selected from the group consisting of tin and lead. % Or more 45
Consists of less than wt% and cadmium. Furthermore, this alloy
It may contain at least one selected from the group consisting of bismuth, indium, calcium, antimony, mercury and silver in a range of 20% by weight or less. By using these alloys, it is possible to reduce gas generation due to decomposition of the electrolyte even when charging and discharging are repeated.
本発明の合金、例えば鉛30重量%,カドミウム70重量%
の合金(以下〔Pb(30)−Cd(70)〕で表わす)を、リ
チウムイオンを含む非水電解質中で負極として使用する
時の充放電反応は(1)式のように表わすことができ
る。Alloys of the invention, eg 30% lead, 70% cadmium
The charge-discharge reaction when the alloy (hereinafter referred to as [Pb (30) -Cd (70)]) is used as a negative electrode in a non-aqueous electrolyte containing lithium ions can be expressed as in equation (1). .
式中〔Pb(30)−Cd(70)〕Lixは、合金中にリチウム
を吸蔵して生成したリチウム合金を示している。また充
放電のできる範囲として、(1)式に表わしたように、
合金中に吸蔵されたリチウムを全て放出して放電する必
要はなく、(2)式に示すように合金中のリチウムの量
を変えて充放電できることは明らかである。この場合、
負極の合金は放電状態においてもリチウムを含んでい
る。 In the formula, [Pb (30) -Cd (70)] Li x represents a lithium alloy produced by occluding lithium in the alloy. In addition, as the range that can be charged and discharged, as shown in equation (1),
It is clear that it is not necessary to discharge all the lithium occluded in the alloy to discharge it, and it is clear that the amount of lithium in the alloy can be changed and the charge and discharge can be performed as shown in the formula (2). in this case,
The alloy of the negative electrode contains lithium even in the discharged state.
実施例の説明 以下の実施例で使用した合金は、すべて溶融時に真空に
引いて、合金中に溶存している酸素,窒素などを取り除
いた。これは、合金を充放電する際に発生する合金中の
溶存ガスの影響を除き、電解質の分解によるガス量を明
確に知るためである。 Description of Examples The alloys used in the following examples were all vacuumed during melting to remove oxygen, nitrogen and the like dissolved in the alloys. This is because the amount of gas due to the decomposition of the electrolyte is clearly known, excluding the influence of the dissolved gas in the alloy generated when charging and discharging the alloy.
実施例1 鉛とカドミウムの合金について、組成を変えて、以下の
実験を行った。Example 1 The following experiment was conducted for lead-cadmium alloys with different compositions.
第1図は電解質の分解により発生するガスを測定するた
めに用いたセルの構成を示す。1は負極としての特性を
評価するための各種合金からなる電極で、大きさ1×1c
m,厚さ0.2mmの合金の両面にニッケルのエキスパンドメ
タルを圧着して構成したものである。2は電極1のリー
ドで、ニッケルよりなる。3は対極で、活物質のMoO3と
導電材のアセチレンブラック,結着剤のポリ四フッ化エ
チレンの混合物を圧縮成形したものである。この電極3
の集電体はチタンであり、リードもチタンリボン4を用
いた。照合電極5にはリチウム板を用い、リードにはニ
ッケルリボン6を使用した。電解質7には1モル/の
過塩素酸リチウムを溶解したプロピレンカーボネートを
使用した。試験極である合金極1と照合電極5には、側
面に孔8を設けた円錐形のガラス容器9をかぶせ、孔を
介して対極との間で電解質のイオン移動が可能となるよ
うにした。10はこれらの電極を入れたガラスセル、11は
封口に用いたシリコーンゴム栓である。実験の開始時に
は、ガス捕集用の円錐形のガラス容器9の頂点に、ガス
がないようにした。FIG. 1 shows the configuration of a cell used for measuring the gas generated by decomposition of the electrolyte. 1 is an electrode made of various alloys for evaluating the characteristics as a negative electrode, and has a size of 1 × 1c
It is made by crimping expanded metal of nickel on both sides of an alloy of m and 0.2 mm in thickness. Reference numeral 2 denotes a lead of the electrode 1, which is made of nickel. Reference numeral 3 is a counter electrode, which is formed by compression-molding a mixture of MoO 3 as an active material, acetylene black as a conductive material, and polytetrafluoroethylene as a binder. This electrode 3
The current collector was titanium, and the lead used the titanium ribbon 4. A lithium plate was used for the reference electrode 5, and a nickel ribbon 6 was used for the lead. As the electrolyte 7, propylene carbonate in which 1 mol / liter of lithium perchlorate was dissolved was used. The alloy electrode 1 as the test electrode and the reference electrode 5 were covered with a conical glass container 9 having a hole 8 on the side surface so that the ions of the electrolyte could be transferred between the counter electrode and the counter electrode through the hole. . 10 is a glass cell containing these electrodes, and 11 is a silicone rubber stopper used for sealing. At the beginning of the experiment, there was no gas at the top of the conical glass container 9 for collecting gas.
測定セルを上述のようにした後、試験極の電位が照合電
極であるリチウムとの間で0.05Vになるまで2mAで充電
し、充電終了後0.8Vになるまで2mAで放電した。さらに
この充放電をくり返した。この時のガス捕集用のガラス
容器9の頂点にたまるガス量を測定した。After the measurement cell was set as described above, it was charged with 2 mA until the potential of the test electrode reached 0.05 V with respect to the reference electrode lithium and discharged with 2 mA until it reached 0.8 V after completion of charging. Further, this charging / discharging was repeated. At this time, the amount of gas accumulated at the apex of the glass container 9 for collecting gas was measured.
前述の充放電サイクルでは、合金の組成により充放電量
は変化する。一般に合金中のカドミウム量が少ない程充
放電量は大きい。In the above charge / discharge cycle, the charge / discharge amount changes depending on the composition of the alloy. Generally, the smaller the amount of cadmium in the alloy, the larger the charge / discharge amount.
従って、合金からのガス発生量を比較するために、各サ
イクルの放電量の和である累積放電量に対して、発生し
た累積ガス量を比較した。これにより、同一累積放電
量、すなわち定電流であることより同一放電時間までに
発生したガス量を比較することになる。Therefore, in order to compare the gas generation amount from the alloys, the generated cumulative gas amount was compared with the cumulative discharge amount which is the sum of the discharge amounts in each cycle. As a result, the same cumulative discharge amount, that is, the amount of gas generated by the same discharge time by the constant current is compared.
第2図は、用いた鉛−カドミウム合金中のカドミウムの
含量に対して、累積放電量が3Ahの時の累積ガス発生量
を比較したものである。これより合金中の鉛量が50重量
%以下、特に45重量%未満でガス発生は少なくなること
がわかる。FIG. 2 compares the amount of cadmium contained in the lead-cadmium alloy used with the cumulative amount of gas generated when the cumulative amount of discharge was 3 Ah. From this, it can be seen that when the lead content in the alloy is 50% by weight or less, particularly less than 45% by weight, gas generation is reduced.
実施例2 合金には、スズ−カドミウム合金を用いて、実施例1と
同様の検討を行った。なお電解質は1モール/の硼フ
ッ化リチウム(LiBF4)を溶解したγ−ブチロラクトン
を用いた。発生したガスは、分子中に炭素と水素を有す
ることより、溶媒のγ−ブチロラクトンが分解したもと
推定される。Example 2 A tin-cadmium alloy was used as the alloy, and the same examination as in Example 1 was conducted. The electrolyte used was γ-butyrolactone in which 1 mol / liter of lithium borofluoride (LiBF 4 ) was dissolved. Since the generated gas has carbon and hydrogen in the molecule, it is presumed that the solvent γ-butyrolactone is decomposed.
第3図は累積放電量が3Ahの時の累積ガス発生量と、合
金中のカドミウムの含量をプロットして示す。この合金
でもスズ量が45重量%未満でガス発生は低下することが
わかる。FIG. 3 is a plot showing the cumulative gas generation amount and the cadmium content in the alloy when the cumulative discharge amount is 3 Ah. It can be seen that even with this alloy, gas generation is reduced when the tin content is less than 45% by weight.
実施例3 合金には、スズ−鉛−カドミウム3元合金を用いた。合
金中のスズと鉛は同一量とし、カドミウムの量を変えて
検討した。電解質にはプロピレンカーボネートと1,2−
ジメトキシエタンの体積比で1対1の混合溶媒に過塩素
酸リチウム1モル/を溶解したものを用いた。発生す
るガスは、分子中に炭素と水素を有することより溶媒が
分解したものと推定される。Example 3 A tin-lead-cadmium ternary alloy was used as the alloy. The amounts of tin and lead in the alloy were the same, and the amount of cadmium was changed and examined. Propylene carbonate and 1,2-
A solution obtained by dissolving 1 mol / liter of lithium perchlorate in a mixed solvent having a volume ratio of dimethoxyethane of 1: 1 was used. The generated gas is presumed to be a solvent decomposed because it has carbon and hydrogen in the molecule.
第4図は、合金中のカドミウム含量と、累積放電容量が
3Ahの時の累積ガス発生量をプロットしている。この合
金でも、鉛、スズが45重量%未満でガス発生量が少なく
なることがわかる。Fig. 4 shows the cadmium content in the alloy and the cumulative discharge capacity.
The cumulative gas generation amount at 3 Ah is plotted. It can be seen that even with this alloy, the amount of gas generated is reduced when the content of lead and tin is less than 45% by weight.
以上から非水電解質の溶媒の分解には、主にスズや鉛が
関与しており、このスズや鉛の量を45%未満にすること
によりガス発生量は少なくなることがわかる。さらに第
2図から第4図では、カドミウムの量が55重量%付近よ
りガス発生は顕著に低下している。このことからカドミ
ウムがガス発生に何らかの抑制作用を持っていることも
推定される。From the above, it is understood that tin and lead are mainly involved in the decomposition of the solvent of the non-aqueous electrolyte, and the gas generation amount is reduced by making the amount of tin or lead less than 45%. Further, in FIGS. 2 to 4, the gas generation is remarkably reduced when the amount of cadmium is around 55% by weight. From this, it is estimated that cadmium has some inhibitory effect on gas generation.
カドミウムは公害物質であることから、できるだけ使用
量は少ない方が良い。カドミウムの一部を他の金属で置
き換えて、ガス発生への影響を調べた結果を以下に説明
する。Since cadmium is a pollutant, it is better to use as little as possible. The results of investigating the effect on gas generation by replacing a part of cadmium with another metal will be described below.
実施例4 スズ,鉛の群から選んだ少なくとも1種と、カドミウム
を必須要素とし、さらにこれに水銀,銀,インジウム,
カルシウム,アンチモン,ビスマスの群から選んだ少な
くとも1種を加えた合金について検討した。実施例とし
て示す合金として、スズまたは鉛が40重量%で、ビスマ
ス,水銀,銀,インジウム,カルシウム,アンチモンの
群から選んだ1種の量を20重量%とし、残部をカドミウ
ムとした。Example 4 At least one selected from the group consisting of tin and lead, and cadmium are essential elements, and mercury, silver, indium, and
An alloy containing at least one selected from the group consisting of calcium, antimony and bismuth was studied. As an alloy shown as an example, tin or lead was 40% by weight, an amount of one selected from the group of bismuth, mercury, silver, indium, calcium and antimony was 20% by weight, and the balance was cadmium.
実施例1と同様の条件で試験した。次表には、累積放電
量が3Ahとなった時の累積ガス発生量を示した。これよ
り、ビスマス,水銀,インジウム,銀を添加することに
よりガス発生は少なくなる。またカルシウム,アンチモ
ンを添加することにより、わずかではあるがガス発生が
少なくなることがわかる。The test was conducted under the same conditions as in Example 1. The following table shows the cumulative gas generation rate when the cumulative discharge rate reached 3 Ah. From this, gas generation is reduced by adding bismuth, mercury, indium, and silver. It is also found that the addition of calcium and antimony reduces gas generation, albeit slightly.
合金中に、水銀,銀,アンチモン,カルシウム,インジ
ウムを添加すると、充放電をくり返した時の各サイクル
の充放電量は増加する。したがって合金中のカドミウム
をインジウム,ビスマス,水銀,銀,アンチモン,カル
シウムで置き換えると充放電量は増加し、またガス発生
量も低下することがわかった。これは、これらの添加金
属にガス発生に対する抑制作用があるためと推定でき
る。しかし、鉛やスズが多いと、インジウム,ビスマ
ス,水銀,銀,アンチモン,カルシウムを添加すること
によるガス発生抑止の効果は小さかった。これらの金属
の添加効果は、スズ,鉛の量が45重量%未満の時に現わ
れてくる。 Addition of mercury, silver, antimony, calcium, and indium to the alloy increases the charge / discharge amount in each cycle when charge / discharge is repeated. Therefore, it was found that when cadmium in the alloy was replaced with indium, bismuth, mercury, silver, antimony, and calcium, the charge / discharge amount increased and the gas generation amount also decreased. This can be presumed to be because these added metals have a suppressing effect on gas generation. However, when the amount of lead and tin is large, the effect of suppressing gas generation by adding indium, bismuth, mercury, silver, antimony, and calcium was small. The effect of adding these metals appears when the amount of tin and lead is less than 45% by weight.
以上の例では、対極にMoO3を用いたが、活性炭を用いた
場合にも有効であり、その他充放電の可逆性を有する正
極を用いられる。以上のように合金中のスズや鉛量を少
なくすることにより、ガス発生を抑制することが可能と
なるが、先に述べたように、充放電に直接かかわるスズ
や鉛の量が少なくなると充放電量の低下が起こる。In the above examples, MoO 3 was used as the counter electrode, but it is also effective when activated carbon is used, and a positive electrode having reversibility of charge / discharge can be used. As described above, by reducing the amount of tin and lead in the alloy, it is possible to suppress gas generation, but as mentioned earlier, when the amount of tin and lead, which are directly involved in charging and discharging, decreases. The amount of discharge decreases.
再充電可能な充放電装置の充放電量は、正極と負極の充
放電量によって決まる。特に実施例で述べたMoO3よりな
る正極の場合には、正極の充放電量は100mAh/cc以上と
大きい。一方、活性炭を正極に用いた場合には、充放電
量は2mAh/cc以下と小さい。とくに活性炭を正極に用い
た場合には、正極の充放電量が小さいため、負極の充放
電量は、高率放電をしても250mAh/cc以上あれば、電気
化学装置の充放電量は、ほとんど正極の充放電容量のみ
で決まる。つまり電気化学装置内部を全て活性炭で充填
した状態の充放電量に近い値が得られることになる。The charge / discharge amount of the rechargeable charge / discharge device is determined by the charge / discharge amount of the positive electrode and the negative electrode. In particular, in the case of the positive electrode made of MoO 3 described in the examples, the charge / discharge amount of the positive electrode is as large as 100 mAh / cc or more. On the other hand, when activated carbon is used for the positive electrode, the charge / discharge amount is as small as 2 mAh / cc or less. Especially when activated carbon is used for the positive electrode, the charge and discharge amount of the positive electrode is small, so if the charge and discharge amount of the negative electrode is 250 mAh / cc or more even at high rate discharge, the charge and discharge amount of the electrochemical device is: Almost determined by the charge and discharge capacity of the positive electrode. In other words, a value close to the charge / discharge amount when the inside of the electrochemical device is filled with activated carbon can be obtained.
これより負極の合金組成としては、鉛やスズの量が10重
量%のものでも使用できることになる。As a result, the alloy composition of the negative electrode can be used even if the amount of lead or tin is 10% by weight.
発明の効果 以上のように、本発明によれば、非水電解質の溶媒の分
解によるガス発生の少ない負極を得ることができる。従
って、特に充放電寿命の長い密閉系電気化学装置に有用
である。EFFECTS OF THE INVENTION As described above, according to the present invention, it is possible to obtain a negative electrode with less gas generation due to the decomposition of the solvent of the non-aqueous electrolyte. Therefore, it is particularly useful for a closed electrochemical device having a long charge / discharge life.
第1図は本発明の実施例を用いたセルの縦断面図、第2
図,第3図及び第4図は各種合金のCd含量と累積ガス発
生量との関係を示す図である。FIG. 1 is a vertical sectional view of a cell using an embodiment of the present invention, and FIG.
FIGS. 3, 3 and 4 are diagrams showing the relationship between the Cd content of various alloys and the cumulative gas generation amount.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 飯島 孝志 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭55−43737(JP,A) 日経エレクトロニクス、第339号(昭59 −3−26)P.93−94 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Takashi Iijima 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP 55-43737 (JP, A) Nikkei Electronics, No. 339 (Showa 59-3-26) P. 93-94
Claims (1)
オンを吸蔵してアルカリ金属との合金を作り、放電によ
りアルカリ金属イオンとして電解質中に放出する合金か
らなる再充電可能な電気化学装置用負極であって、前記
負極の合金が、スズ及び鉛よりなる群から選んだ少なく
とも1種の10重量%以上45重量%未満と、インジウム、
カルシウム、アンチモン、水銀及び銀よりなる群から選
んだ少なくとも1種の20重量%以下(ただし0を含まな
い)と、残部のカドミウムからなる合金である再充電可
能な電気化学装置用負極。1. A rechargeable negative electrode for an electrochemical device comprising an alloy which absorbs an alkali metal ion in a non-aqueous electrolyte to form an alloy with an alkali metal by charging and which is released into the electrolyte as an alkali metal ion by discharging. The alloy of the negative electrode is at least 10% by weight or more and less than 45% by weight of at least one selected from the group consisting of tin and lead, and indium,
A rechargeable negative electrode for an electrochemical device, which is an alloy composed of 20% by weight or less (not including 0) of at least one selected from the group consisting of calcium, antimony, mercury, and silver, and the balance of cadmium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59107804A JPH0782838B2 (en) | 1984-05-28 | 1984-05-28 | Rechargeable negative electrode for electrochemical device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59107804A JPH0782838B2 (en) | 1984-05-28 | 1984-05-28 | Rechargeable negative electrode for electrochemical device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60253155A JPS60253155A (en) | 1985-12-13 |
| JPH0782838B2 true JPH0782838B2 (en) | 1995-09-06 |
Family
ID=14468453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59107804A Expired - Lifetime JPH0782838B2 (en) | 1984-05-28 | 1984-05-28 | Rechargeable negative electrode for electrochemical device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0782838B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5543737A (en) * | 1978-09-20 | 1980-03-27 | Seiko Instr & Electronics Ltd | Button-type alkaline battery and its manufacturing method |
-
1984
- 1984-05-28 JP JP59107804A patent/JPH0782838B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| 日経エレクトロニクス、第339号(昭59−3−26)P.93−94 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60253155A (en) | 1985-12-13 |
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