JPH0425670B2 - - Google Patents

Info

Publication number
JPH0425670B2
JPH0425670B2 JP59196746A JP19674684A JPH0425670B2 JP H0425670 B2 JPH0425670 B2 JP H0425670B2 JP 59196746 A JP59196746 A JP 59196746A JP 19674684 A JP19674684 A JP 19674684A JP H0425670 B2 JPH0425670 B2 JP H0425670B2
Authority
JP
Japan
Prior art keywords
zinc powder
zinc
powder
hydrogen gas
gas generation
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
Application number
JP59196746A
Other languages
Japanese (ja)
Other versions
JPS6177264A (en
Inventor
Nobuyori Kasahara
Keiichi Kagawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Kinzoku Co Ltd
Original Assignee
Mitsui Mining and Smelting Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Mining and Smelting Co Ltd filed Critical Mitsui Mining and Smelting Co Ltd
Priority to JP59196746A priority Critical patent/JPS6177264A/en
Publication of JPS6177264A publication Critical patent/JPS6177264A/en
Publication of JPH0425670B2 publication Critical patent/JPH0425670B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • H01M4/12Processes of manufacture of consumable metal or alloy electrodes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明はアルカリ電池用亜鉛粉に関し、詳しく
はタンニン酸またはイミダゾールで亜鉛粉の表面
を処理し、キレート皮膜を生成させることによ
り、未処理の亜鉛粉に比較し、水素ガス発生を著
しく抑制したアルカリ電池用亜鉛粉に関する。 [従来の技術] 単位重量当りの電気量が大きく、化学的にも比
較的安定で、加工性に富み、安価であることから
アルカリ電池の陰極活物質として専らアトマイズ
された亜鉛粉が賞用されている。 しかし、アルカリ電解液の中では亜鉛の化学的
溶解によつて電池内にガスが蓄積して圧力が上昇
し、電解液の漏出や、電池の変形、はなはだしい
ときには電池の破壊が起こることがある。その対
策として、従来では水銀の水素過電圧を利用した
汞化亜鉛粉が負極活物質として用いられている。
このため、今日市販されているアルカリ電池の負
極活物質は5〜10%重量%程度の多量の水銀を含
有しており、社会的ニーズとしてより低水銀の電
池、あるいは無水銀の電池の開発が強く期待され
るようになつてきた。 そこで電池内の水銀含有率を低減させるべく、
水銀以外の亜鉛の水素ガス発生を抑制する元素を
添加した各種亜鉛粉が提案されているが、いずれ
も水素ガス発生率を抑制するのには充分ではなく
未だに水銀の使用を避け得ぬ現状にある。 [発明が解決しようとする課題] 本発明は上記のような状況に鑑み、これら亜鉛
粉の水素ガス発生抑制効果をさらに大きくした亜
鉛粉を提供することを目的とする。 [課題を解決するための手段] 本発明者らは上記目的を達成するために種々研
究したところ、各種亜鉛粉を亜鉛とキレート化合
物をつくる有機化合物であるタンニン酸やイミダ
ゾールが溶解している溶液中で表面処理すること
により、未処理の亜鉛粉に比較し、水素ガス発生
が著しく抑制されるという知見を得て本発明に至
つた。 すなわち本発明は、苛性アルカリ水溶液を電解
液とするアルカリ電池の負極用亜鉛粉において、
タンニン酸やイミダゾールで表面処理を施すこと
により得られるアルカリ電池用亜鉛粉にある。 本発明において使用される亜鉛粉とは、亜鉛の
粉末のみならず、鉛やインジウムで合金化した亜
鉛合金粉やこれら亜鉛粉、亜鉛合金粉を汞化した
汞化亜鉛粉、汞化亜鉛合金粉も包含される。 本発明においては、タンニン酸またはイミダゾ
ールで亜鉛粉の表面を処理し、キレート皮膜を生
成する。また、このタンニン酸等による亜鉛粉の
表面処理の前処理として、亜鉛粉の表面を塩酸、
酢酸等の酸または水酸化カリウム、水酸化ナトリ
ウム等のアルカリの溶液で処理することによつ
て、水素ガス発生の抑制効果が一層促進される。 本発明が水素ガス発生を抑制するという効果を
有する理由については明白ではないが、以下の理
由が考えられる。 通常、亜鉛粉はアトマイズ法で製造されている
が、この方法であれば、一般に表面は粗面となり
表面にキズや微細な凹凸を生じやすい。腐食の観
点から、これらの部分は活性点となり腐食を促進
する。すなわち水素ガス発生が生じやすいはずで
あるが、タンニン酸やイミダゾールで表面処理を
することにより、亜鉛粉の極表面層がキレート生
成反応により溶解し、新たな平滑度の高い表面状
態となると同時に、生成したキレート化合物の皮
膜が耐食性をもたらし、結果として水素ガス発生
を抑制すると考えられる。 ここで亜鉛粉表面に形成されたキレート化合物
皮膜については、干渉色の生成により確認できる
こともあるが、1μの厚さ以下の極く薄い皮膜と
推定され、亜鉛粉の放電特性には何等影響をもた
らさないことも確認されている。なお、上述のご
とく、本発明は亜鉛合金粉、汞化亜鉛粉、汞化亜
鉛合金粉にも適用可能である。これらのキレート
反応も電池反応と同様に亜鉛の表面層の酸化反応
により皮膜が生成されるためと考えられる。 [実施例] 以下、本発明を亜鉛粉調製例、実施例および比
較例に基づき具体的に説明するが、処理条件、供
用亜鉛粉等はこれに限定されるものではない。 亜鉛粉調整例 純度99.997%以上の亜鉛地金を約500℃で溶融
して、第1表に示す組成並びに含有率になるよう
に元素(Pb、In、Tl)を添加して亜鉛合金を作
成しこれを高圧空気ガス(噴出圧5Kg/cm2)を用
いてアトマイズ粉を作成した。次いで50〜150メ
ツシユになるように篩別し、亜鉛粉(a)および亜鉛
粉(b)を調製した。 また、亜鉛粉(a)を用いてアルカリ水溶液中にて
汞化させ、水銀含有率1.0重量%の汞化亜鉛粉で
ある亜鉛粉(c)を調製した。 実施例 1 純水にタンニン酸を溶解し、10g/のタンニ
ン酸溶液1を作成した。この溶液中に亜鉛粉(a)
を1Kg投入し、50℃にて30撹拌しながら表面処理
を行なつた。次いで水洗を5回繰返し、濾過後、
45℃で一昼夜乾燥させ、本発明の亜鉛粉(実施例
1)を得た。 このようにして得られた亜鉛粉を用いて水素ガ
ス発生試験を行なつた。その試験方法は電解液と
して濃度40重量%の水酸化カリウム水溶液に酸化
亜鉛を飽和させたもの5ml、亜鉛粉10gを用いて
45℃で30日間のガス発生量を測定した。この結果
を第1表に示す。 実施例 2〜4 1:10HCI溶液1中に亜鉛粉(a)、亜鉛粉(b)お
よび亜鉛粉(c)をそれぞれ1Kg投入し、常温にて10
分間撹拌を行なつた。次に傾潟水洗を行ない、
pHが2程度の亜鉛粉入り希HCI溶液0.5とし
た。次いで、予め作成済の10g/タンニン酸溶
液を投入して、常温にて60分撹拌しながら表面処
理を行なつた。その後水洗を5回繰返し、濾過
後、45℃で一昼夜乾燥させ、本発明の亜鉛粉(実
施例2〜4)を得た。 このようにして得られた亜鉛粉を用いて、実施
例1と同様な方法により水素ガス発生試験を行な
つた。この結果を第1表に示す。 実施例 5〜6 亜鉛粉(a)および亜鉛粉(c)を用い、タンニン酸の
代わりにイミダゾールを用いる以外は実施例1と
同様な方法で本発明の亜鉛粉(実施例5〜6)を
得た。 このようにして得られた亜鉛粉を用いて、実施
例1と同様に方法により水素ガス発生試験を行な
つた。この結果を第1表に示す。 比較例 1〜3 亜鉛粉(a)、亜鉛粉(b)および亜鉛粉(c)を何らの処
理を施さずに、実施例1と同様な方法により水素
ガス発生試験を行なつた。その結果を第1表に示
す。 比較例 4 亜鉛粉(a)を用い、タンニン酸の代わりにシユウ
酸ナトリウムを用いる以外は実施例1と同様な方
法で亜鉛粉(比較例4)を得た。 このようにして得られた亜鉛粉を用いて、実施
例1と同様な方法により水素ガス発生試験を行な
つた。この結果を第1票に示す。 比較例 5 亜鉛粉(a)を用い、タンニン酸の代わりにシユウ
酸ナトリウムを用いる以外は実施例2と同様な方
法で亜鉛粉(比較例5)を得た。 このようにして得られた亜鉛粉を用いて、実施
例1と同様な方法により水素ガス発生試験を行な
つた。この結果を第1表に示す。
[Industrial Application Field] The present invention relates to zinc powder for alkaline batteries, and more specifically, by treating the surface of zinc powder with tannic acid or imidazole to form a chelate film, it has a higher hydrogen resistance than untreated zinc powder. This invention relates to zinc powder for alkaline batteries that significantly suppresses gas generation. [Prior art] Atomized zinc powder has been used exclusively as a cathode active material for alkaline batteries because it has a large amount of electricity per unit weight, is relatively stable chemically, has good processability, and is inexpensive. ing. However, in an alkaline electrolyte, chemical dissolution of zinc causes gas to accumulate inside the battery and increase pressure, which can cause leakage of the electrolyte, deformation of the battery, and in extreme cases, destruction of the battery. As a countermeasure against this, conventionally, zinc chloride powder, which utilizes the hydrogen overvoltage of mercury, has been used as a negative electrode active material.
For this reason, the negative electrode active materials of alkaline batteries commercially available today contain a large amount of mercury, approximately 5% to 10% by weight, and social needs call for the development of lower mercury or mercury-free batteries. It has become highly anticipated. Therefore, in order to reduce the mercury content in batteries,
Various zinc powders have been proposed that contain elements other than mercury that suppress hydrogen gas generation from zinc, but none of them are sufficient to suppress the hydrogen gas generation rate, and the use of mercury is still unavoidable. be. [Problems to be Solved by the Invention] In view of the above-mentioned circumstances, an object of the present invention is to provide zinc powder that further increases the hydrogen gas generation suppressing effect of these zinc powders. [Means for Solving the Problems] In order to achieve the above object, the present inventors conducted various studies and found that various zinc powders were dissolved in a solution containing tannic acid and imidazole, which are organic compounds that form chelate compounds with zinc. The present invention was based on the finding that hydrogen gas generation is significantly suppressed by surface treatment in zinc powder compared to untreated zinc powder. That is, the present invention provides zinc powder for negative electrodes of alkaline batteries using an aqueous caustic solution as an electrolyte.
Zinc powder for alkaline batteries obtained by surface treatment with tannic acid or imidazole. The zinc powder used in the present invention is not only zinc powder, but also zinc alloy powder alloyed with lead or indium, zinc alloy powder made of these zinc powders, zinc alloy powder made of zinc alloy powder, and zinc alloy powder made of zinc alloy powder. is also included. In the present invention, the surface of zinc powder is treated with tannic acid or imidazole to form a chelate film. In addition, as a pretreatment for the surface treatment of zinc powder with tannic acid, etc., the surface of the zinc powder is treated with hydrochloric acid.
The effect of suppressing hydrogen gas generation is further promoted by treatment with an acid such as acetic acid or an alkali solution such as potassium hydroxide or sodium hydroxide. Although it is not clear why the present invention has the effect of suppressing hydrogen gas generation, the following reasons can be considered. Zinc powder is usually produced by the atomization method, but this method generally results in a rough surface, which tends to cause scratches and fine irregularities on the surface. From a corrosion perspective, these parts act as active sites and promote corrosion. In other words, hydrogen gas should be easily generated, but by surface treatment with tannic acid or imidazole, the extreme surface layer of the zinc powder is dissolved by a chelate formation reaction, creating a new highly smooth surface condition. It is thought that the resulting chelate compound film provides corrosion resistance and, as a result, suppresses hydrogen gas generation. The chelate compound film formed on the surface of the zinc powder can sometimes be confirmed by the generation of interference colors, but it is estimated to be an extremely thin film with a thickness of less than 1μ, and has no effect on the discharge characteristics of the zinc powder. It has also been confirmed that it does not. As mentioned above, the present invention is also applicable to zinc alloy powder, zinc chloride powder, and zinc chloride alloy powder. It is thought that these chelate reactions also produce a film due to the oxidation reaction of the surface layer of zinc, similar to the battery reaction. [Example] The present invention will be specifically described below based on zinc powder preparation examples, examples, and comparative examples, but the processing conditions, zinc powder used, etc. are not limited thereto. Zinc powder preparation example Zinc alloy is created by melting zinc ingot with a purity of 99.997% or higher at approximately 500℃ and adding elements (Pb, In, Tl) to the composition and content shown in Table 1. This powder was atomized using high-pressure air gas (ejection pressure: 5 kg/cm 2 ). Next, the powder was sieved to a size of 50 to 150 meshes to prepare zinc powder (a) and zinc powder (b). Further, the zinc powder (a) was aqueous in an alkaline aqueous solution to prepare zinc powder (c), which is a aqueous zinc powder with a mercury content of 1.0% by weight. Example 1 Tannic acid was dissolved in pure water to prepare 10 g/tannic acid solution 1. Zinc powder (a) in this solution
1 kg of was added, and the surface treatment was carried out at 50°C while stirring for 30 minutes. Next, the water washing was repeated 5 times, and after filtration,
It was dried at 45° C. for a day and night to obtain zinc powder of the present invention (Example 1). A hydrogen gas generation test was conducted using the zinc powder thus obtained. The test method was to use 5 ml of a potassium hydroxide aqueous solution with a concentration of 40% by weight saturated with zinc oxide and 10 g of zinc powder as the electrolyte.
The amount of gas generated was measured at 45°C for 30 days. The results are shown in Table 1. Examples 2 to 4 1 kg of zinc powder (a), zinc powder (b), and zinc powder (c) were each added to 1:10 HCI solution 1, and the mixture was heated to 1 kg at room temperature.
Stirring was performed for a minute. Next, perform tilting water washing,
A dilute HCI solution containing zinc powder with a pH of about 2 was used. Next, 10 g/tannic acid solution prepared in advance was added, and the surface treatment was performed while stirring at room temperature for 60 minutes. Thereafter, washing with water was repeated five times, and after filtration, it was dried at 45° C. for a day and night to obtain zinc powder of the present invention (Examples 2 to 4). Using the zinc powder thus obtained, a hydrogen gas generation test was conducted in the same manner as in Example 1. The results are shown in Table 1. Examples 5-6 Zinc powder of the present invention (Examples 5-6) was prepared in the same manner as in Example 1 except that zinc powder (a) and zinc powder (c) were used and imidazole was used instead of tannic acid. Obtained. Using the zinc powder thus obtained, a hydrogen gas generation test was conducted in the same manner as in Example 1. The results are shown in Table 1. Comparative Examples 1 to 3 A hydrogen gas generation test was conducted in the same manner as in Example 1, without subjecting zinc powder (a), zinc powder (b), and zinc powder (c) to any treatment. The results are shown in Table 1. Comparative Example 4 Zinc powder (Comparative Example 4) was obtained in the same manner as in Example 1 except that zinc powder (a) was used and sodium oxalate was used instead of tannic acid. Using the zinc powder thus obtained, a hydrogen gas generation test was conducted in the same manner as in Example 1. This result is shown in the first vote. Comparative Example 5 Zinc powder (Comparative Example 5) was obtained in the same manner as in Example 2 except that zinc powder (a) was used and sodium oxalate was used instead of tannic acid. Using the zinc powder thus obtained, a hydrogen gas generation test was conducted in the same manner as in Example 1. The results are shown in Table 1.

【表】 第1表に示されるごとく、亜鉛粉(a)、亜鉛粉(b)
および亜鉛粉(c)をタンニン酸またはイミダゾール
で表面処理を行なつた実施例1〜6の亜鉛粉は、
亜鉛粉(a)、亜鉛粉(b)および亜鉛粉(c)に何ら処理を
施さなかつた比較例1〜3に比較して水素ガス発
生が著しく抑制されている。 また、比較例4〜5は、実施例1〜2のタンニ
ン酸に代えてシユウ酸ナトリウムを用いたもので
あるが、水素ガス発生の抑制効果は実施例1〜2
に比べて劣る。 [発明の効果] 以上説明のごとく、タンニン酸またはイミダゾ
ールで亜鉛粉の表面を処理し、キレート皮膜をそ
の表面に生成した本発明のアルカリ電池用亜鉛粉
は、水素ガス発生を著しく抑制することから、ア
ルカリ電池の負極として好適に用いられ、その工
業的価値は大である。
[Table] As shown in Table 1, zinc powder (a), zinc powder (b)
The zinc powders of Examples 1 to 6, in which the zinc powder (c) was surface-treated with tannic acid or imidazole, were
Hydrogen gas generation is significantly suppressed compared to Comparative Examples 1 to 3 in which zinc powder (a), zinc powder (b), and zinc powder (c) were not subjected to any treatment. Furthermore, in Comparative Examples 4 and 5, sodium oxalate was used in place of tannic acid in Examples 1 and 2, but the effect of suppressing hydrogen gas generation was that of Examples 1 and 2.
inferior to. [Effects of the Invention] As explained above, the zinc powder for alkaline batteries of the present invention, in which the surface of the zinc powder is treated with tannic acid or imidazole to form a chelate film on the surface, significantly suppresses hydrogen gas generation. It is suitably used as a negative electrode for alkaline batteries and has great industrial value.

Claims (1)

【特許請求の範囲】 1 苛性アルカリ水溶液を電解液とするアルカリ
電池の負極用亜鉛粉において、タンニン酸または
イミダゾールで表面処理を施すことにより得られ
るアルカリ電池用亜鉛粉。 2 前記表面処理の前処理として、亜鉛粉を酸ま
たはアルカリで処理する前記特許請求の範囲第1
項記載のアルカリ電池用亜鉛粉。
[Scope of Claims] 1. Zinc powder for alkaline batteries obtained by surface-treating zinc powder for negative electrodes of alkaline batteries using an aqueous caustic alkali solution as an electrolyte with tannic acid or imidazole. 2. Claim 1, wherein the zinc powder is treated with acid or alkali as a pretreatment for the surface treatment.
Zinc powder for alkaline batteries as described in .
JP59196746A 1984-09-21 1984-09-21 Zinc powder for alkaline battery Granted JPS6177264A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59196746A JPS6177264A (en) 1984-09-21 1984-09-21 Zinc powder for alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59196746A JPS6177264A (en) 1984-09-21 1984-09-21 Zinc powder for alkaline battery

Publications (2)

Publication Number Publication Date
JPS6177264A JPS6177264A (en) 1986-04-19
JPH0425670B2 true JPH0425670B2 (en) 1992-05-01

Family

ID=16362914

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59196746A Granted JPS6177264A (en) 1984-09-21 1984-09-21 Zinc powder for alkaline battery

Country Status (1)

Country Link
JP (1) JPS6177264A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63279569A (en) * 1987-05-12 1988-11-16 Fuji Elelctrochem Co Ltd Alkaline battery
JPH07123042B2 (en) * 1987-05-12 1995-12-25 富士電気化学株式会社 Alkaline battery
US6284410B1 (en) 1997-08-01 2001-09-04 Duracell Inc. Zinc electrode particle form

Also Published As

Publication number Publication date
JPS6177264A (en) 1986-04-19

Similar Documents

Publication Publication Date Title
JPH035024B2 (en)
JP2770396B2 (en) Zinc alkaline battery
JPH0425670B2 (en)
JPH031784B2 (en)
JP3178160B2 (en) Method for producing negative electrode for button-type alkaline battery and button-type alkaline battery
JPS61109256A (en) Zinc anode of alkaline call
JP2737233B2 (en) Zinc alkaline battery
JPS58225565A (en) Alkaline battery
EP0162411A2 (en) Process for the production of active anode materials for use in cells
JP3708198B2 (en) Negative electrode for alkaline batteries
JP2737231B2 (en) Zinc alkaline battery
JP2737230B2 (en) Zinc alkaline battery
JPH0317181B2 (en)
JP2737232B2 (en) Zinc alkaline battery
JPS5842740A (en) Zinc alloy for electrode
JPS61253764A (en) Zinc alkaline battery
JP2805486B2 (en) Alkaline battery and its negative electrode active material
JP2805489B2 (en) Alkaline battery and its negative electrode active material
JPS58181266A (en) Negative active material for battery and its manufacture
JPS61203563A (en) Alkaline zinc battery
JPH04206266A (en) Zinc alloy for zinc alkaline battery, its manufacture and relative zinc alkaline battery
JPS6273565A (en) Zinc alkaline battery
JP2805485B2 (en) Alkaline battery and its negative electrode active material
JPH01279564A (en) Manufacture of amalgamated zinc alloy powder
JPS6316553A (en) Zinc alkaline battery