JPS609081B2 - Manufacturing method of spheroidized subgrain - Google Patents
Manufacturing method of spheroidized subgrainInfo
- Publication number
- JPS609081B2 JPS609081B2 JP10078782A JP10078782A JPS609081B2 JP S609081 B2 JPS609081 B2 JP S609081B2 JP 10078782 A JP10078782 A JP 10078782A JP 10078782 A JP10078782 A JP 10078782A JP S609081 B2 JPS609081 B2 JP S609081B2
- Authority
- JP
- Japan
- Prior art keywords
- metal
- zinc
- particles
- oxygen
- hopper
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 27
- 229910052760 oxygen Inorganic materials 0.000 claims description 27
- 239000001301 oxygen Substances 0.000 claims description 27
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 22
- 229910052725 zinc Inorganic materials 0.000 claims description 21
- 239000011701 zinc Substances 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 15
- 239000002245 particle Substances 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 4
- 239000002923 metal particle Substances 0.000 description 27
- 229910052751 metal Inorganic materials 0.000 description 25
- 239000002184 metal Substances 0.000 description 25
- 239000003595 mist Substances 0.000 description 10
- 238000000889 atomisation Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- 238000007711 solidification Methods 0.000 description 5
- 230000008023 solidification Effects 0.000 description 5
- 229910052793 cadmium Inorganic materials 0.000 description 4
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000012798 spherical particle Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910001111 Fine metal Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000009689 gas atomisation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F9/082—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
Landscapes
- Glanulating (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Description
【発明の詳細な説明】
本発明は、金属粒の製造方法に関するものであり、特に
は微細な球状金属粒を簡易効率的に製造する方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing metal particles, and particularly to a method for producing fine spherical metal particles simply and efficiently.
球状の金属粒を製造する方法としては、冷却媒体への滴
下法或いは気体贋霧により得られた金属粒をスパラル管
を通して気流搬送することにより形状修正を行なう物理
的球状化法が提唱されている。As a method for manufacturing spherical metal particles, a physical spheroidization method has been proposed in which the shape is modified by dropping metal particles into a cooling medium or by transporting metal particles obtained by gas mist through a spral tube. .
しかしながら、冷却媒体への滴下法で金属粒を製造する
場合には、粒寸の小さいものが得られず、例えば100
メッシュ以上の粒が90%近くまでも占め、100メッ
シュ以下の微細な金属粒の製造方法としては適当でない
。However, when producing metal particles by dropping into a cooling medium, small particle sizes cannot be obtained;
The particles with a mesh size or larger account for nearly 90%, and this method is not suitable as a method for producing fine metal particles with a mesh size of 100 mesh or smaller.
また、上記した金属溶体を気体贋移した後スパイラル管
を通過させる方法は、尖鋭突起を無くする点である程度
の効果があるとは云え、球状と言えるにはまだ尚不足し
ており、加えて装置の構造が複雑となるばかりか、操業
管理が煩雑である。In addition, although the above-mentioned method of passing the metal solution through a spiral tube after transferring the gas has some effect in eliminating sharp protrusions, it is still insufficient to be called spherical. Not only does the structure of the device become complicated, but operation management is also complicated.
従って、従来からの提唱方法は、微細な球状金属粒を得
るには満足すべきものと言い難い。ところで、近時、亜
鉛、カドミウム、鉛、鋼等の金属粒において微細な球状
形態のものを製造することが、粉末成形体の品質向上等
の目的から、強く要望されている。例えばアルカリ電池
においては、最近ますます小型化及び薄型化に進む額向
があり、電池寿命を長くする対策として電極成型体に用
いられる亜鉛が微粒子であり且つ球状であることが要望
されている。このような微粒球状の金属粒製造は上記の
ような方法では得ることが難しく、新たな方法の確立が
必要である。本発明は、上記従来技術の欠点を解消する
と共に、斯界での要望に答えるべく微粒の球状金属粒を
容易に製造する方法を確立したものである。Therefore, the conventionally proposed methods cannot be said to be satisfactory for obtaining fine spherical metal particles. Incidentally, in recent years, there has been a strong demand for producing fine spherical particles of metal such as zinc, cadmium, lead, steel, etc. for the purpose of improving the quality of powder compacts. For example, alkaline batteries are becoming increasingly smaller and thinner, and as a measure to extend battery life, it is desired that the zinc used in electrode moldings be fine particles and spherical. It is difficult to produce such fine, spherical metal particles using the methods described above, and it is necessary to establish a new method. The present invention has established a method for easily manufacturing fine spherical metal particles in order to eliminate the drawbacks of the above-mentioned prior art and to meet the demands in this field.
本発明者は、金属溶体を噂霧気体により紬滴に分散させ
る気体燈霧法について、金属粒の生成状況を仔細に観察
検討した結果、金属溶瓶が凝固するまでの間に生成する
酸化物が球状化の成否の鍵をにぎり、酸化物量が所定量
を越えると球状化が阻まれることを知見した。金属容体
溜め容器から落下する金属溶体は頃霧気体により贋霧化
されて溶滴として分散し、金属粒回収ホッパ内を落下し
つつ凝固してその底に溜まるのであるが、その過程での
金属溶体と酸素との結びつく機会を所定限以下に抑制す
ることが必要である。そのためには、贋霧気体中の酸素
濃度はもちろんのこと、金属粒回収ホッパ内の酸素濃度
をも所定限度以下に維持することが必要である。酸素濃
度の上限は、対象とする金属に依存はするが、球状化の
程度の観察から8%とするのが一般である。The inventor of the present invention has carefully observed and studied the formation of metal particles in the gas vaporization method, in which a metal solution is dispersed into pongee droplets using a mist gas. It was discovered that the key to the success or failure of spheroidization is that spheroidization is inhibited when the amount of oxide exceeds a predetermined amount. The metal solution falling from the metal storage container is atomized by the mist gas and dispersed as droplets, and as it falls through the metal particle collection hopper, it solidifies and accumulates at the bottom, but in the process, metal It is necessary to suppress the chance of bonding of the solution and oxygen to below a predetermined limit. For this purpose, it is necessary to maintain not only the oxygen concentration in the falsified gas but also the oxygen concentration in the metal particle collection hopper below a predetermined limit. Although the upper limit of the oxygen concentration depends on the metal in question, it is generally set at 8% based on the observation of the degree of spheroidization.
斯くして、本発明は、金属溶体を頃霧気体により紬滴に
分散せしめ、そして金属粒回収ホッパ内を落下せしめて
瓶集することから成る金属粒製造方法において、贋霧気
体中の酸素濃度及び金属粒回収ホッパ内雰囲気の酸素濃
度を8%以下とすることを特徴とする金属粒製造方法を
提供する。In this way, the present invention provides a method for producing metal particles, which comprises dispersing a metal solution into droplets using mist gas, allowing them to fall through a metal particle collection hopper and collecting them in a bottle, in which the oxygen concentration in the mist gas is reduced. The present invention also provides a method for producing metal particles, characterized in that the oxygen concentration in the atmosphere within the metal particle recovery hopper is 8% or less.
以下、本発明について詳細に述べる。本発明において対
象とする金属は頃霧法により金属粒を製造しうる金属一
般をすべて含むものであるが、特に酸素との親和力の高
い、例えば亜鉛、カドミウム、鉛或いはこれらの合金等
の金属が対象とされる。The present invention will be described in detail below. The metals targeted in the present invention include all metals in general from which metal particles can be produced by the rolling method, but metals that have a high affinity for oxygen, such as zinc, cadmium, lead, or alloys thereof, are particularly targeted. be done.
金属溶体は、金属粒回収ホッパ上に設置された溜め容器
において所定の温度に維持されつつその底に設けられた
ノズルを通して放出され、放出直後頃霧気体によって細
滴に分散される。The metal solution is maintained at a predetermined temperature in a storage container installed on the metal particle collection hopper and released through a nozzle provided at the bottom of the storage container, and immediately after release, it is dispersed into fine droplets by a mist gas.
分散した紬滴はホッパ内を落下しつつ凝固し、そしてホ
ッパ底において金属粒として橘集される。金属熔体の温
度は、融点にできることだけ近いほどよいが、頃霧化が
可能な範囲の温度にあることを要する。The dispersed pongee droplets solidify as they fall within the hopper, and are collected as metal particles at the bottom of the hopper. The temperature of the metal melt should be as close to the melting point as possible, but it must be within a temperature range that allows atomization.
例えば、電池用の亜鉛粒製造の場合には、最純亜鉛(9
9.99%Zn)が用いられ、溶体温度は450〜60
0午0とされる。溶体の温度は噴霧化紬滴の凝固時間と
相関するから、細滴がホッパ壁に衝突する際充分に凝固
していないと衝撃によって偏平化或いは歪曲化しやすい
ので、ホツパ壁への衝突までに充分の凝固粒が得られる
よう、設備の他の因子を考慮して港体温度を選定するこ
とが望まれる。ホッパの容積が大きく、ホツパ壁に分散
紬滴が衝突するまでの時間が比較的長くとれる場合には
、溶体温度を高くすることができる。しかし、大形のホ
ッパの使用は設備がかさむ点で好ましくないので、溶体
温度を低目することが好ましい。ホツパの側壁は曲面を
呈することが好ましい。For example, in the case of manufacturing zinc particles for batteries, the purest zinc (9
9.99% Zn) was used, and the solution temperature was 450-60
It is considered to be 0:00. Since the temperature of the solution is correlated with the solidification time of the atomized droplets, if the fine droplets are not sufficiently solidified when they collide with the hopper wall, they are likely to become flattened or distorted by the impact. It is desirable to select the port body temperature in consideration of other factors of the equipment so as to obtain coagulated particles of If the hopper has a large volume and the time required for the dispersed pongee droplets to collide with the hopper wall is relatively long, the solution temperature can be increased. However, since the use of a large hopper is undesirable because it requires bulky equipment, it is preferable to keep the solution temperature low. Preferably, the side wall of the hopper has a curved surface.
これは前述したように噴霧化金属が側壁に当るまでに充
分冷却されていないと変形しやすいので、曲面とするこ
とによって衝撃を少しでも綾らげるためである。噂霧気
体圧力は、紬粒を得るには高い程良いが、あまり高くし
すぎると側壁等に分散溶滴が当って変形したり或いは圧
力衝撃によって溶滴が偏平になるのでかえって好ましく
ない。This is because, as mentioned above, if the atomized metal is not sufficiently cooled before it hits the side wall, it is likely to deform, so the curved surface reduces the impact as much as possible. The higher the atomization gas pressure is, the better in order to obtain pongee grains, but if it is set too high, the dispersed droplets may hit the side walls and deform, or the droplets may become flat due to pressure impact, which is not preferable.
なるだけ一様なそして微細な頃霧化効果が得られるよう
溜め容器底の放出ノズル寸法等をも勘案して適正な圧力
を選定する必要がある。例えば、亜鉛の場合では、一般
に1〜5k9/地の範囲とされ、2k9/地が好ましい
。本発明に従えば、贋霧気体は酸素濃度は8%以下に抑
制されることを要する。In order to obtain as uniform and fine atomization effect as possible, it is necessary to select an appropriate pressure, taking into consideration the dimensions of the discharge nozzle at the bottom of the reservoir, etc. For example, in the case of zinc, it generally ranges from 1 to 5k9/ground, with 2k9/ground being preferred. According to the present invention, the oxygen concentration of the mist gas must be suppressed to 8% or less.
これは、金属溶体と酸素との接触する機会をできる限り
少なくするためである。填霧気体としては、噴霧ガス、
C02ガス、アルゴンその他の不活性ガスが用いられる
。特に本発明において重要なことは、噴霧化後細適が未
凝固状態で滞留する金属粒回収ホッパ内雰囲気の酸素濃
度をも8%以下に管理することである。This is to minimize the chance of contact between the metal solution and oxygen. As the atomizing gas, atomizing gas,
C02 gas, argon and other inert gases are used. Particularly important in the present invention is to control the oxygen concentration in the atmosphere within the metal particle collection hopper, where the particles remain in an unsolidified state after atomization, to 8% or less.
従来装置においては、このホッパ内のフリーエアー雰囲
気の管理が不十分若しくはほとんど配慮されず、特にそ
の酸素濃度を厳密に限定することは行われず、これが球
状の金属粒を得られなかった重大原因であったと思われ
る。従来装置においては、溶体溜め容器と回収ホッパと
の間から周囲空気が侵入しやすく、ホッパ内雰囲気の酸
素濃度はかなり高いものと推察される。従って、本発明
においては、ホッパ内部が外部と密閉性の良い構造をと
る必要がある。溶体溜め容器とホッパとの連結部及び金
属粒回収口に適宜の密閉手段を設けねばならない。こう
して、最小限の酸素接触下で頃霧化された分散細滴は、
それらが凝固し終るまで酸素との接触を最小限に絶たれ
、以つて、酸化物がほとんど生成されない状態で表面張
力により球状化する。In conventional equipment, the free air atmosphere inside the hopper was poorly controlled or little consideration was given, and the oxygen concentration was not strictly limited, which was a major reason why spherical metal particles could not be obtained. It seems that there was. In the conventional apparatus, ambient air easily enters between the solution reservoir and the recovery hopper, and it is assumed that the oxygen concentration in the atmosphere inside the hopper is quite high. Therefore, in the present invention, it is necessary that the inside of the hopper has a structure that is well sealed from the outside. Appropriate sealing means must be provided at the connection between the solution reservoir and the hopper and at the metal particle collection port. Thus, the dispersed droplets are atomized under minimal oxygen contact.
Contact with oxygen is minimized until they have solidified, and then they become spheroidized due to surface tension with little oxide formation.
酸化物が所定以上あると、液滴の表面張力、粘性等に悪
影響を及ぼして充分なる球状化効果が発現しない。この
ように、金属溶体の贋霧化から凝固までに至る期間、金
属と酸素との接触を最小限に抑えることこそ一層球状化
した金属粒を得る為に最重要な要件であり、従釆はここ
まで綿密な考慮が払われていなかったのである。If the amount of oxide exceeds a predetermined amount, it will adversely affect the surface tension, viscosity, etc. of the droplets, and a sufficient spheroidizing effect will not be achieved. In this way, minimizing the contact between the metal and oxygen during the period from atomization to solidification of the metal solution is the most important requirement in order to obtain more spherical metal particles. Such careful consideration had not been given.
酸素濃度の上限の限定は、先にも少し触れたように、対
象金属の酸素親和力の程度に依存はするが、金属全般に
対して8%以下(零も含む)であ*れば充分であること
が見出された。As mentioned earlier, the upper limit of the oxygen concentration depends on the degree of oxygen affinity of the target metal, but it is sufficient if it is 8% or less (including zero) for all metals. Something was discovered.
この限界値は、各種金属に対してカサ比重を測定するこ
と及び顕微鏡観察により球状化の程度の把握することに
より為された。例えば酸素との親和力の強い亜鉛の場合
、次のような結果が得られた。カサ密度は、金属粒が整
粒のものであり且つ球状Z化する程大きくなり、金属粒
の性状に関してきわめて明確なめやすを与えるものであ
り、本発明と関連しては3.20を超えるものが優秀と
判定された。This limit value was determined by measuring bulk specific gravity of various metals and understanding the degree of spheroidization through microscopic observation. For example, in the case of zinc, which has a strong affinity for oxygen, the following results were obtained. The bulk density increases as the metal grains are of regular size and become spherical, and provides a very clear indication of the properties of the metal grains. was judged to be excellent.
参考写真1及び2の対比からわかるように、酸2素濃度
の減少による球状化効果はまさに驚くべきものであり、
従来品が細長く異形であったのに較べ、酸素濃度を厳密
に管理することによりカサ比重の大きい整流球状化金属
粒が得られる。As can be seen from the comparison between Reference Photos 1 and 2, the spheroidization effect due to the decrease in oxygen concentration is truly amazing.
Compared to conventional products, which were elongated and irregularly shaped, by strictly controlling the oxygen concentration, rectified spheroidal metal particles with a large bulk specific gravity can be obtained.
また、本発明に従って製造された金属粒は例えば一般に
求められる100〜200メッシュのものが多い微細な
ものである。上記考慮に加えて、噂霧気体の温度も最終
金属粒製品に影響を及ぼす。Further, the metal particles produced according to the present invention are usually fine particles with a mesh size of 100 to 200, which is generally required. In addition to the above considerations, the temperature of the atomizing gas also affects the final metal particulate product.
溜め容器ノズルから流下する金属落陽に対して、贋霧気
体による急激な冷却作用は、充分には解明されていない
が、粘性、局所的凝固等の因子と関連して良好な球状化
をもたらされない。従って、昇温された曙霧気体の使用
も本発明の目的に好作用を及ぼす。しかし、あまりに高
温の贋霧気体の使用は、かえって金属滴の凝固を遅らせ
しかも排ガス温度が高くなりバグフィルタ等の簡易な収
塵設備の使用ができなくなるので好ましくない。次に亜
鉛溶湯を使用しての実施例並びに比較例を述べる。The rapid cooling effect of the mist gas on the metal falling from the reservoir nozzle is not fully understood, but it is thought to be related to factors such as viscosity and local solidification, resulting in good spheroidization. Not done. Therefore, the use of a warmed-up mist gas also has a favorable effect on the objectives of the present invention. However, it is not preferable to use a false mist gas that is too high in temperature because it will actually delay the solidification of the metal droplets and will also raise the temperature of the exhaust gas, making it impossible to use simple dust collection equipment such as bag filters. Next, examples and comparative examples using molten zinc will be described.
例噴霧気体として所定の酸素濃度に調節された常温の窒
素+酸素ガスを使用してアルカIJ電池用の亜鉛粒の製
造を行った。Example Zinc particles for an Alka IJ battery were manufactured using room temperature nitrogen + oxygen gas adjusted to a predetermined oxygen concentration as the atomizing gas.
カサ比重3.320以上の100〜200メッシュの球
状粒を生成することを目標とした。実施条件及び結果は
次の通りである;上表からわかるように、酸素濃度を8
%以下に管理することによって3.20以上のカサ比重
を有する亜鉛粒が生成され、これは非常に整粒され且つ
球状化された亜鉛粒が生成されることを意味する。また
、冷却媒体への滴下法とは対照的に、特にアルカリ電池
に要求される100〜200メッシュの微細な粒が高い
占有率で生成された。こうして本発明により生成された
亜鉛粒はカサ比重が従来品より約1.劫音程大きくなる
ため、アルカリ電池等小型電池の能力アップに著しい貢
献をなすものである。また、アルカリ電池においては、
従来一定の粒蚤のものが得られず、また細長い形態のも
のが大多数であったため(参考写真1)、亜鉛線を一定
形状のものに切断することも行われていたが、本発明に
より一定寸の球状のものがそのような面倒な方法に依ら
ず、簡単な頃霧法によって連続的に製造しうろことも大
きなメリットである。更には、電池用原料としての亜鉛
粒は不純物成分としての酸素が嫌われるが、酸素量の少
ない亜鉛粒が本発明によって同時的に縛られることも、
本発明の好ましい結果の一つである。以上のことはカド
ミ電池用のカドミウム粒等に対しても該当する。以上説
明した通り、本発明は、従釆ほとんど配慮されることの
なかった金陣溶体の頃霧化から凝固に至るまでの過程全
体を通しての酸素との接触を厳密に管理することにより
、気体噴霧法によって簡易に且つ効率的に微細な球状金
属粒の製造を可能ならしめたものである。The aim was to produce spherical particles of 100 to 200 mesh with a bulk specific gravity of 3.320 or more. The implementation conditions and results are as follows; as can be seen from the table above, the oxygen concentration was
% or less, zinc grains having a bulk specific gravity of 3.20 or more are produced, which means that zinc grains that are highly sized and spheroidized are produced. Furthermore, in contrast to the method of dropping into a cooling medium, fine particles of 100 to 200 mesh, which are particularly required for alkaline batteries, were produced at a high occupancy rate. The bulk specific gravity of the zinc particles thus produced according to the present invention is about 1. Since the kalpa pitch becomes larger, it makes a significant contribution to increasing the capacity of small batteries such as alkaline batteries. In addition, in alkaline batteries,
Conventionally, zinc wire could not be obtained with a uniform grain size, and the majority of the wires were long and thin (reference photo 1), so zinc wire was cut into uniform shapes, but with the present invention, It is also a great advantage that spherical objects of a certain size can be manufactured continuously by a simple spraying method without relying on such troublesome methods. Furthermore, zinc grains used as a raw material for batteries do not like oxygen as an impurity component, but the present invention also binds zinc grains with a small amount of oxygen at the same time.
This is one of the preferable results of the present invention. The above also applies to cadmium particles for cadmium batteries. As explained above, the present invention enables gas atomization by strictly controlling contact with oxygen throughout the entire process from atomization to solidification, which was rarely considered in the past. This method makes it possible to easily and efficiently produce fine spherical metal particles.
Claims (1)
て亜鉛粒回収ホツパ内を落下せしめて捕集することから
成る亜鉛粒製造方法において、噴霧気体中の酸素濃度及
び亜鉛粒回収ホツパ内雰囲気の酸素濃度を8%以下とす
ることにより球状化亜鉛粒を生成することを等徴とする
球状化亜鉛粒の製造方法。1. In a method for manufacturing zinc particles, which consists of dispersing zinc solution into fine droplets using atomized gas, and then allowing them to fall and be collected in a zinc particle recovery hopper, the oxygen concentration in the atomized gas and the oxygen in the atmosphere inside the zinc particle recovery hopper are A method for producing spheroidized zinc particles, which is characterized by producing spheroidized zinc particles by controlling the concentration to 8% or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10078782A JPS609081B2 (en) | 1982-06-14 | 1982-06-14 | Manufacturing method of spheroidized subgrain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10078782A JPS609081B2 (en) | 1982-06-14 | 1982-06-14 | Manufacturing method of spheroidized subgrain |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58217607A JPS58217607A (en) | 1983-12-17 |
| JPS609081B2 true JPS609081B2 (en) | 1985-03-07 |
Family
ID=14283155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10078782A Expired JPS609081B2 (en) | 1982-06-14 | 1982-06-14 | Manufacturing method of spheroidized subgrain |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS609081B2 (en) |
-
1982
- 1982-06-14 JP JP10078782A patent/JPS609081B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58217607A (en) | 1983-12-17 |
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