JPS61221311A - Production of zinc powder for negative electrode of alkaline cell - Google Patents

Production of zinc powder for negative electrode of alkaline cell

Info

Publication number
JPS61221311A
JPS61221311A JP5946385A JP5946385A JPS61221311A JP S61221311 A JPS61221311 A JP S61221311A JP 5946385 A JP5946385 A JP 5946385A JP 5946385 A JP5946385 A JP 5946385A JP S61221311 A JPS61221311 A JP S61221311A
Authority
JP
Japan
Prior art keywords
zinc
molten
powder
negative electrode
atmosphere
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP5946385A
Other languages
Japanese (ja)
Inventor
Kazuo Furushima
古嶋 和夫
Kazumasa Yoshida
和正 吉田
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.)
FDK Twicell Co Ltd
Original Assignee
Toshiba Battery 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 Toshiba Battery Co Ltd filed Critical Toshiba Battery Co Ltd
Priority to JP5946385A priority Critical patent/JPS61221311A/en
Publication of JPS61221311A publication Critical patent/JPS61221311A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PURPOSE:To produce zinc or zinc alloy powder for a negative electrode of an alkaline cell having a large surface area and excellent heavy load discharge characteristic by spraying molten zinc or molten zinc alloy into an atmosphere in which the oxygen concn. is higher than the oxygen concn. in air. CONSTITUTION:High-purity Zn or Zn alloy formed by adding positively a prescribed ratio each of Al, Mn, Pb, Sn, Cd, Tl, Bi, etc. thereto is melted. The molten Zn or molten Zn alloy is then sprayed into the atmosphere in which the oxygen concn. is higher than the oxygen concn. of the air. The zinc oxide is formed on the surface of the molten drops formed in the above-mentioned manner and at the same time the molten drops are cooled and solidified, by which the Zn or Zn alloy powder having he large surface area is obtd. The negative electrode of the alkaline cell having the excellent heavy load discharge characteristic is formed by using such powder.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明はアルカリ電池の負極として用いられる亜鉛又は
亜鉛合金粉末の製造方法に関し、更に詳しくは、重負荷
放電特性に優れた亜鉛又は亜鉛合金粉末の製造方法に関
する。
Detailed Description of the Invention [Technical Field of the Invention] The present invention relates to a method for producing zinc or zinc alloy powder used as a negative electrode for alkaline batteries, and more specifically, to a method for producing zinc or zinc alloy powder that has excellent heavy load discharge characteristics. Regarding the manufacturing method.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

電解液が苛性カリ、苛性ンーダのようなアルカリ水溶液
であるアルカリ電池の負極として使用される亜鉛粉末又
は亜鉛合金粉末は、概ね、次のよりにして製造されてい
る。すなわち、溶融亜鉛又は溶融亜鉛合金を、空気中又
は酸素濃度が空気の場合よυも低い還元性雰囲気中罠噴
霧して微粉とし、更にこの微粉を水又は亜鉛溶解性水溶
液の中に浸漬しこれを攪拌しながら金属水銀又は塩化第
二水銀のような可溶性水銀塩で表面氷化する、という方
法である。
Zinc powder or zinc alloy powder used as the negative electrode of an alkaline battery whose electrolyte is an alkaline aqueous solution such as caustic potash or caustic powder is generally produced as follows. That is, molten zinc or molten zinc alloy is trap-sprayed into a fine powder in air or in a reducing atmosphere where the oxygen concentration is lower than air, and then this fine powder is immersed in water or a zinc-soluble aqueous solution. This method involves freezing the surface of the sample with metallic mercury or a soluble mercury salt such as mercuric chloride while stirring.

しかしながら、上記方法で負極用粉末を製造し九場合、
溶融噴霧時の酸素濃度が低いため、得られた微粉表面の
亜鉛酸化物の量が少なくなるという利点の反面、微粉の
表面積が小さくなるという問題が生ずる。しかも、上記
した水化処理時に亜鉛表面の溶解反応や攪拌などによる
微粉間の相互摩耗によってその表面積は一層減少する。
However, when producing negative electrode powder using the above method,
Since the oxygen concentration during melt spraying is low, there is an advantage that the amount of zinc oxide on the surface of the obtained fine powder is reduced, but on the other hand, there is a problem that the surface area of the fine powder is reduced. Moreover, during the above-mentioned hydration treatment, the surface area of the zinc is further reduced due to mutual abrasion between the fine powders due to the dissolution reaction on the zinc surface and stirring.

このように表面積が小さくなるということは、亜鉛又は
亜鉛合金粉末の負極としての全体的な反応面積が減少す
ることであって、そのことは電池特性における重負荷放
電特性低下の原因を構成する。
This reduction in surface area means that the overall reaction area of the zinc or zinc alloy powder as a negative electrode is reduced, which is the cause of the deterioration of heavy load discharge characteristics in the battery characteristics.

〔発明の目的〕[Purpose of the invention]

本発明は、上記した問題を解消して、電極反応に寄与す
る負極亜鉛又は亜鉛合金粉末の表面積を犬たらしめ、も
って重負荷放電を可能たらしめる亜鉛又は亜鉛合金粉末
を製造する方法の提供を目的とする。
The present invention solves the above-mentioned problems and provides a method for manufacturing zinc or zinc alloy powder that reduces the surface area of negative electrode zinc or zinc alloy powder that contributes to electrode reactions, thereby making heavy load discharge possible. purpose.

〔発明の概要〕[Summary of the invention]

本発明者らは、上記目的を達成すべく鋭意研究を重ねた
結果、亜鉛又は亜鉛合金を溶融噴霧したとき、得られる
粉末の比表面積(単位重量当シの表面積)は周辺雰囲気
の酸素濃度によって影響を受けるとの事実、更には酸素
濃度が高くなると比表面積も大きくなるとの事実を見出
し、本発明方法を開発するに到った。
As a result of intensive research to achieve the above object, the present inventors found that when zinc or zinc alloy is melted and sprayed, the specific surface area (surface area per unit weight) of the powder obtained depends on the oxygen concentration of the surrounding atmosphere. Based on the findings that the specific surface area increases as the oxygen concentration increases, the method of the present invention was developed.

すなわち、本発明のアルカリ電池用負極亜鉛粉末の製造
方法は、溶融亜鉛又は溶融亜鉛合金を、酸素濃度が空気
中の酸素濃度より高い雰囲気の中に噴霧することを特徴
とする。
That is, the method for producing negative electrode zinc powder for alkaline batteries of the present invention is characterized by spraying molten zinc or molten zinc alloy into an atmosphere in which the oxygen concentration is higher than the oxygen concentration in the air.

本発明方法においては、まず、高純度の亜鉛又はこれに
積極的にアルミニウム、マンガン、鉛、スズ、カドミウ
ム、タリウム、ビスマスなどの元素を所定量添加して成
る亜鉛合金を溶融する。ついでこの溶融亜鉛又は溶融亜
鉛合金を、後述する雰囲気中に噴霧して粉末にする。こ
のときの溶融噴霧の方法は、例えば特開昭50−484
27号公報に開示されている装置を用いて行なうことが
好ましく、この装置の注下ルツボ孔径、噴霧ノズルの交
叉角等の条件を適宜選定することにより所望する粒径、
形状の粉末を製造することができる。
In the method of the present invention, first, high-purity zinc or a zinc alloy formed by actively adding a predetermined amount of elements such as aluminum, manganese, lead, tin, cadmium, thallium, and bismuth to the zinc is melted. This molten zinc or molten zinc alloy is then sprayed into an atmosphere described below to form a powder. The method of melt spraying at this time is, for example, Japanese Patent Application Laid-Open No. 50-484
It is preferable to use the apparatus disclosed in Publication No. 27, and by appropriately selecting conditions such as the diameter of the pouring crucible hole and the intersection angle of the spray nozzle, the desired particle size,
It is possible to produce powders in the following shapes.

適用する雰囲気は、酸素濃度が空気中のそれよりも高い
雰囲気である。具体的には、空気中の酸素濃度は約20
.9 vo/チであるから、酸素濃度20.9 vod
 %より高い雰囲気である。
The applied atmosphere is one in which the oxygen concentration is higher than that in air. Specifically, the oxygen concentration in the air is approximately 20
.. Since it is 9 vo/chi, the oxygen concentration is 20.9 vod
The atmosphere is higher than %.

このように酸素濃度が高い雰囲気中に亜鉛又は亜鉛合金
を溶融噴霧すると、その理由付けは必ずしも明確ではな
いが、形成された粉末d比表面積は大きくなる。おそら
く、次のような理由に基づくのではないかと推考される
。すなわち、溶融亜鉛又は溶融亜鉛合金を噴霧すると、
雰囲気中の酸素によって形成され九融滴の粉末の表面に
は亜鉛酸化物が生成する。形成された融滴の粉末は同時
的に冷却されていくが、そのとき粉末の表面は凝縮する
。この凝縮過程で、表面に生成した酸化物の量の多寡に
より凝縮の程度に差異が生じひいては表面積の差を引起
すものと考えられる。
When zinc or zinc alloy is molten and sprayed into an atmosphere with such a high oxygen concentration, the d-specific surface area of the formed powder increases, although the reasoning is not necessarily clear. It is assumed that this is probably based on the following reasons. That is, when spraying molten zinc or molten zinc alloy,
Zinc oxide is formed on the surface of the powder of the nine melt droplets, which is formed by the oxygen in the atmosphere. The formed molten droplet powder is simultaneously cooled, and at this time the surface of the powder condenses. In this condensation process, it is thought that the degree of condensation varies depending on the amount of oxide produced on the surface, which in turn causes a difference in surface area.

いずれにしても、雰囲気中の酸素濃度が空気中のそれ以
下になると、得られた粉末の比表面積が減少して電極反
応に寄与する反応面積の減少を招き、重負荷放電特性を
向上せしめない。
In any case, if the oxygen concentration in the atmosphere is lower than that in air, the specific surface area of the obtained powder will decrease, resulting in a decrease in the reaction area that contributes to electrode reactions, and heavy load discharge characteristics will not be improved. .

〔発明の実施例〕[Embodiments of the invention]

純度99.99 %の亜鉛を石英ルツゲに入れ、全体を
アルゴン雰囲気中にて温度600℃で溶融した。融液を
充分攪拌したのち、特開昭50−48427号公報に開
示されている装置を用いた気体噴霧法で微粉化した。こ
のとき、噴霧時における雰囲気の酸素濃度をかえて各種
の亜鉛粉末を調製しその比表面積を測定した。
Zinc with a purity of 99.99% was placed in a quartz glass and the whole was melted at a temperature of 600°C in an argon atmosphere. After thoroughly stirring the melt, it was pulverized by a gas atomization method using an apparatus disclosed in Japanese Patent Application Laid-Open No. 50-48427. At this time, various zinc powders were prepared by changing the oxygen concentration of the atmosphere during spraying, and their specific surface areas were measured.

なお、比表面積の測定は、電気化学協会主催の第24回
電池討論会(昭和58年)の要旨集129頁に記載され
ている方法で行なった。
The specific surface area was measured by the method described on page 129 of the abstracts of the 24th Battery Symposium (1981) sponsored by the Electrochemical Society of Japan.

その結果を、空気中(酸素濃度20.9 vol % 
)噴霧時の比表面積(SA)に対する各酸素濃度雰囲気
中噴霧時の比表面積(S□)の比(So/SA)として
示した。
The results are shown in air (oxygen concentration 20.9 vol%).
) It is expressed as the ratio (So/SA) of the specific surface area (S□) when spraying in each oxygen concentration atmosphere to the specific surface area (SA) when spraying.

第 1 表 つぎに各亜鉛粉末を弱酸性の塩化第二水銀水溶液に浸漬
してこれを攪拌し、水銀の氷化率5重量−である水化亜
鉛粉末を得た。酸化亜鉛を飽和させた40チ水酸化カリ
ウム水溶液を電解液とし、対極はニッケル板、基準電極
に水銀、・酸化水銀電極を用いてハーフセルを製作した
Table 1 Next, each zinc powder was immersed in a weakly acidic mercuric chloride aqueous solution and stirred to obtain zinc hydrate powder having a mercury freezing rate of 5% by weight. A half cell was fabricated using a 40% potassium hydroxide aqueous solution saturated with zinc oxide as the electrolyte, a nickel plate as the counter electrode, mercury as the reference electrode, and a mercury oxide electrode.

このハーフセルを第2表に示した定電流で放電した。そ
のときの放電持続時間(hr)を測定し、その値を理論
容量で除した値、すなわち亜鉛の利用率(9))を算出
した。その結果を第2表に示し九。
This half cell was discharged at the constant current shown in Table 2. The discharge duration (hr) at that time was measured, and the value divided by the theoretical capacity, that is, the zinc utilization rate (9)) was calculated. The results are shown in Table 2.

第2表 〔発明の効果〕 以上の説明で明らかなように、本発明方法によれば、従
来の方法で製造した亜鉛又は亜鉛合金粉末よpもその表
面積が大きい粉末を製造することができ、したがってそ
れを用いたアルカリ電池の重負荷放電特性は優れたもの
となる。
Table 2 [Effects of the Invention] As is clear from the above explanation, according to the method of the present invention, powder having a larger surface area than zinc or zinc alloy powder produced by the conventional method can be produced. Therefore, an alkaline battery using the same has excellent heavy load discharge characteristics.

Claims (1)

【特許請求の範囲】[Claims] 溶融亜鉛又は溶融亜鉛合金を、酸素濃度が空気中の酸素
濃度より高い雰囲気の中に噴霧することを特徴とするア
ルカリ電池用負極亜鉛粉末の製造方法。
A method for producing negative electrode zinc powder for alkaline batteries, which comprises spraying molten zinc or molten zinc alloy into an atmosphere in which the oxygen concentration is higher than that of air.
JP5946385A 1985-03-26 1985-03-26 Production of zinc powder for negative electrode of alkaline cell Pending JPS61221311A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5946385A JPS61221311A (en) 1985-03-26 1985-03-26 Production of zinc powder for negative electrode of alkaline cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5946385A JPS61221311A (en) 1985-03-26 1985-03-26 Production of zinc powder for negative electrode of alkaline cell

Publications (1)

Publication Number Publication Date
JPS61221311A true JPS61221311A (en) 1986-10-01

Family

ID=13114031

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5946385A Pending JPS61221311A (en) 1985-03-26 1985-03-26 Production of zinc powder for negative electrode of alkaline cell

Country Status (1)

Country Link
JP (1) JPS61221311A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1113419C (en) * 1996-02-22 2003-07-02 尤密考公司 Process for manufacturing primary zinc-alkaline battery and anode mix used therein

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1113419C (en) * 1996-02-22 2003-07-02 尤密考公司 Process for manufacturing primary zinc-alkaline battery and anode mix used therein

Similar Documents

Publication Publication Date Title
JPH10265225A (en) Manufacturing device of metallic hydroxide for battery component
JPH11292547A (en) Lithium cobaltate, its production and lithium cell using that
US4579791A (en) Cell anode
GB2141357A (en) Method for making irregular shaped single crystal particles and the use therof in anodes for electrochemical cells
JP3656353B2 (en) Method for producing positive electrode active material for alkaline storage battery
JPS61221311A (en) Production of zinc powder for negative electrode of alkaline cell
Kao et al. Corrosion resistant coating for a positive lead/acid battery electrode
NL8600347A (en) METHOD FOR THE PRODUCTION OF AN ELECTROCHEMICAL CELL WITH REDUCED GASES AND ELECTROCHEMICAL CELL
JP4852713B2 (en) Zinc alloy powder for alkaline batteries and method for producing the same
JPH04237952A (en) Manufacture of unamalgamated zinc alloy powder for alkaline dry battery
JPH04198028A (en) Lithium manganese double oxide, its production and use
JPS61116755A (en) Zinc powder for alkaline manganese battery and alkaline manganese battery
JPS6158164A (en) Zinc alloy powder for negative electrode of nonmercury alkaline battery and its manufacture
CN113130864B (en) Chemical bond enhanced silver ear-shaped porous carbon sphere embedded with monodisperse nano alloy particles and preparation and application thereof
CN1229284A (en) Anode material for use in alkaline manganese cells and process for producing the same
JPS6110861A (en) Alkaline zinc battery
JPS60262352A (en) Alkaline zinc battery
JP2003272615A (en) Zinc alloy powder and alkaline battery using the same
JPS61224267A (en) Manufacture of electrochemical battery and electrochemical battery
JP3136961B2 (en) Method of treating hydrogen storage alloy for batteries
JPH0441468B2 (en)
JPH01279564A (en) Manufacture of amalgamated zinc alloy powder
JPS58218761A (en) Alkaline battery
JPS636747A (en) Zince alkaline battery
JPS6251160A (en) Alkaline battery