JP2001283842A - Zinc alloy powder for alkaline battery and method for producing the same - Google Patents
Zinc alloy powder for alkaline battery and method for producing the sameInfo
- Publication number
- JP2001283842A JP2001283842A JP2000090271A JP2000090271A JP2001283842A JP 2001283842 A JP2001283842 A JP 2001283842A JP 2000090271 A JP2000090271 A JP 2000090271A JP 2000090271 A JP2000090271 A JP 2000090271A JP 2001283842 A JP2001283842 A JP 2001283842A
- Authority
- JP
- Japan
- Prior art keywords
- zinc alloy
- alloy powder
- zinc
- alkaline battery
- amount
- 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.)
- Granted
Links
- 229910001297 Zn alloy Inorganic materials 0.000 title claims abstract description 70
- 239000000843 powder Substances 0.000 title claims abstract description 53
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 40
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000012535 impurity Substances 0.000 claims abstract description 23
- 229910052742 iron Inorganic materials 0.000 claims abstract description 20
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052797 bismuth Inorganic materials 0.000 claims abstract description 14
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052804 chromium Inorganic materials 0.000 claims abstract description 14
- 239000011651 chromium Substances 0.000 claims abstract description 14
- 229910052738 indium Inorganic materials 0.000 claims abstract description 13
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 13
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 8
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 8
- 239000011777 magnesium Substances 0.000 claims abstract description 8
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 7
- 230000000737 periodic effect Effects 0.000 claims abstract description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 46
- 239000011701 zinc Substances 0.000 claims description 39
- 229910052725 zinc Inorganic materials 0.000 claims description 39
- 238000000034 method Methods 0.000 claims description 13
- 229910052746 lanthanum Inorganic materials 0.000 claims description 5
- 229910052727 yttrium Inorganic materials 0.000 claims description 5
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 3
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical group [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 42
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 23
- 229910052751 metal Inorganic materials 0.000 abstract description 18
- 239000002184 metal Substances 0.000 abstract description 18
- 238000000889 atomisation Methods 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 6
- 229910045601 alloy Inorganic materials 0.000 abstract description 5
- 239000000956 alloy Substances 0.000 abstract description 5
- 239000000654 additive Substances 0.000 abstract description 4
- 230000000996 additive effect Effects 0.000 abstract description 4
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 150000002739 metals Chemical class 0.000 abstract 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 16
- 239000002245 particle Substances 0.000 description 16
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 9
- 239000001257 hydrogen Substances 0.000 description 9
- 229910052739 hydrogen Inorganic materials 0.000 description 9
- 239000002994 raw material Substances 0.000 description 8
- 239000011787 zinc oxide Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 235000011118 potassium hydroxide Nutrition 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000005275 alloying Methods 0.000 description 2
- 229910052787 antimony Inorganic materials 0.000 description 2
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 229910052695 Americium Inorganic materials 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910052685 Curium Inorganic materials 0.000 description 1
- 229910052692 Dysprosium Inorganic materials 0.000 description 1
- 229910052691 Erbium Inorganic materials 0.000 description 1
- 229910052693 Europium Inorganic materials 0.000 description 1
- 229910052688 Gadolinium Inorganic materials 0.000 description 1
- 229910052689 Holmium Inorganic materials 0.000 description 1
- 101000650817 Homo sapiens Semaphorin-4D Proteins 0.000 description 1
- 229910052766 Lawrencium Inorganic materials 0.000 description 1
- 229910052765 Lutetium Inorganic materials 0.000 description 1
- 229910052764 Mendelevium Inorganic materials 0.000 description 1
- 229910052779 Neodymium Inorganic materials 0.000 description 1
- 229910052781 Neptunium Inorganic materials 0.000 description 1
- 229910052778 Plutonium Inorganic materials 0.000 description 1
- 229910052777 Praseodymium Inorganic materials 0.000 description 1
- 229910052774 Proactinium Inorganic materials 0.000 description 1
- 229910052772 Samarium Inorganic materials 0.000 description 1
- 102100027744 Semaphorin-4D Human genes 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 229910052771 Terbium Inorganic materials 0.000 description 1
- 229910052776 Thorium Inorganic materials 0.000 description 1
- 229910052775 Thulium Inorganic materials 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 229910052769 Ytterbium Inorganic materials 0.000 description 1
- 229910052768 actinide Inorganic materials 0.000 description 1
- 150000001255 actinides Chemical class 0.000 description 1
- 229910052767 actinium Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- AJGDITRVXRPLBY-UHFFFAOYSA-N aluminum indium Chemical compound [Al].[In] AJGDITRVXRPLBY-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229940075397 calomel Drugs 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical compound Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 239000006148 magnetic separator Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 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
- 238000002156 mixing Methods 0.000 description 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Powder Metallurgy (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】
【課題】 ガス発生が抑制されたアルカリ電池用亜鉛合
金粉末を製造するためには、亜鉛合金粉末中の不純物を
極微量に規制することで達成されていたが、そのように
極微量にすることはコストアップとなり安価な亜鉛合金
粉末を提供できなかった。
【解決手段】 鉄、ニッケル、クロムなどの特定不純物
がある程度混入していても、亜鉛合金組成の改良とアト
マイズ時の単位時間当たりの亜鉛合金溶湯供給量とアト
マイズガス供給量の比を制御すれば水素ガス発生が大幅
に抑制されたアルカリ電池用合金粉末を提供できる。す
なわち、添加金属としてビスマス、インジウムの0.0
01〜1%をベースに、さらには同じ量のアルミニウ
ム、マグネシウムまたは周期表の13(IIIB)族元素を特
定して合金組成を改良し、かつ上記メタル/ガス比を1
〜5kg/Nm3とする。(57) [Problem] To produce a zinc alloy powder for an alkaline battery with suppressed gas generation, which has been achieved by regulating impurities in the zinc alloy powder to a very small amount. The use of a very small amount increases the cost and fails to provide an inexpensive zinc alloy powder. SOLUTION: Even if specific impurities such as iron, nickel and chromium are mixed to some extent, it is possible to improve the zinc alloy composition and control the ratio of the supply amount of the molten zinc alloy and the supply amount of the atomized gas per unit time during atomization. It is possible to provide an alkaline battery alloy powder in which hydrogen gas generation is significantly suppressed. In other words, bismuth and indium as additive metals
On the basis of 0.1 to 1%, the same amount of aluminum, magnesium or group 13 (IIIB) element of the periodic table is specified to improve the alloy composition, and the metal / gas ratio is set to 1%.
55 kg / Nm 3 .
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水素ガス発生を抑
制し、電池特性を向上させたアルカリ電池用亜鉛合金粉
末およびその製造方法に関し、更に詳しくは、添加金属
としてBi、Inをベースに、さらにはAl、Mgまた
は13(IIIB)族元素を含有し、アトマイズの際の単位時
間当たりの亜鉛溶湯供給量とアトマイズガス供給量との
比を規定することで水素ガス発生量の少ない亜鉛合金粉
末を製造することを目的とするものである。この目的に
使用できる13(IIIB)族元素はSc、Y、ランタニド系
列元素のLa、Ce、Pr、Nd、Sm、Eu、Gd、
Tb、Dy、Ho、Er、Tm、YbおよびLu並びに
アクチニド系列のAc、Th、Pa、U、Np、Pu、
Am、Cm、Bk、Cf、Es、Fm、Md、Noおよ
びLrであるが、特にYとLaが好ましい。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a zinc alloy powder for an alkaline battery in which hydrogen gas generation is suppressed and battery characteristics are improved, and a method for producing the same. Further, a zinc alloy powder containing Al, Mg or a group 13 (IIIB) element and having a small amount of hydrogen gas generated by defining the ratio of the supply amount of the molten zinc per unit time and the supply amount of the atomized gas during atomization. Is intended to be manufactured. Group 13 (IIIB) elements that can be used for this purpose include Sc, Y, and lanthanide series elements La, Ce, Pr, Nd, Sm, Eu, Gd,
Tb, Dy, Ho, Er, Tm, Yb and Lu and the actinide series Ac, Th, Pa, U, Np, Pu,
Am, Cm, Bk, Cf, Es, Fm, Md, No and Lr are preferred, and Y and La are particularly preferred.
【0002】[0002]
【従来の技術】従来、電解液が苛性カリのようなアルカ
リ水溶液であるアルカリ電池の負極として使用されるア
ルカリ電池用亜鉛合金粉末は、電気亜鉛などのような工
業的に得られる亜鉛を原料として、少量の添加金属で合
金化した溶湯をアトマイズ法で噴霧して製造している。2. Description of the Related Art Conventionally, zinc alloy powder for an alkaline battery used as a negative electrode of an alkaline battery in which an electrolytic solution is an aqueous alkaline solution such as caustic potash is produced by using industrially obtained zinc such as electric zinc as a raw material. It is manufactured by spraying molten metal alloyed with a small amount of additive metal by the atomizing method.
【0003】このようにして得られた亜鉛合金粉末に
は、合金成分として添加された金属以外に検出される微
量不純物としてクロム、マンガン、鉄、コバルト、ニッ
ケル、銅、銀、カドミウム、アンチモンなどがあり、こ
れらはいずれも亜鉛の腐食を促進し、水素ガス発生を著
しく増大させることは良く知られている。このため例え
ば特公平7−54705では亜鉛粉中の鉄をlppm以
下にすること、特開平3−56637ではニッケル、ク
ロム、アンチモンをlppm以下とし、鉄を20ppm
以下とすること、特開平9−92278にはニッケル、
クロムを0.5ppm以下とすることなどが開示されて
いる。[0003] The zinc alloy powder thus obtained contains chromium, manganese, iron, cobalt, nickel, copper, silver, cadmium, antimony and the like as trace impurities detected in addition to the metal added as an alloying component. It is well known that all of these promote zinc corrosion and significantly increase hydrogen gas generation. Therefore, for example, Japanese Patent Publication No. 7-54705 sets the iron content of zinc powder to 1 ppm or less, and JP-A-3-56637 sets nickel, chromium and antimony to 1 ppm or less and iron to 20 ppm.
The following is described in JP-A-9-92278,
It is disclosed that the chromium content is 0.5 ppm or less.
【0004】しかし、これらの方法で不純物を極微量に
抑えるには、純度の高い原料亜鉛の使用が必要であった
り、製造ラインの雰囲気を厳密に制御したり、亜鉛粉と
接触する部分をテフロン(登録商標)などで表面処理し
たりする必要があった。そのため、製造される亜鉛粉も
コスト的に高価なものとなってしまい、安価に亜鉛粉を
製造する方法が望まれていた。However, in order to minimize impurities by these methods, it is necessary to use a high-purity raw material zinc, strictly control the atmosphere of the production line, or to remove the part in contact with zinc powder with Teflon. (Registered trademark) or the like. Therefore, the zinc powder to be produced is also expensive, and a method for producing zinc powder at low cost has been desired.
【0005】[0005]
【発明が解決しようとする課題】上述のように、ガス発
生が抑制されたアルカリ電池用亜鉛合金粉末を製造する
ためには、亜鉛合金粉末中の不純物を極微量に規制する
ことが一つの有効な手段であったが、不純物を極微量に
規制することはコストアップにつながり、安価にアルカ
リ電池用亜鉛合金粉末を提供できないという欠点があっ
た。As described above, in order to produce a zinc alloy powder for an alkaline battery in which gas generation is suppressed, it is effective to regulate impurities in the zinc alloy powder to a very small amount. However, regulating impurities to a very small amount leads to an increase in cost, and there is a disadvantage that zinc alloy powder for alkaline batteries cannot be provided at low cost.
【0006】亜鉛合金粉末中への不純物の混入は使用す
る原料からの混入以外に次のような経路で混入する。ま
ず、亜鉛合金粉末は通常アトマイズ法にて製造される
が、これは原料である亜鉛を溶解し、所定の合金化金属
を添加した後、溶湯を細流状に流下させ、これに高圧ガ
スを噴射させることによって、粉末状に加工する方法で
ある。アルカリ電池用亜鉛合金粉末は、アトマイズ後の
亜鉛合金粉末を所望の粒度に分級した後、磁選機により
製造ラインから混入した鉄分を除去し、製品としてい
る。この製造方法においては、原料を溶解する工程で、
溶解炉内に残留する鉄分の混入による汚染および原料亜
鉛の溶解にともなうドロス処理の際にドロス処理機材質
からの鉄分やニッケル、クロムの混入による汚染が生じ
る。また、アトマイズ工程で生じた微小融滴が、冷却チ
ャンバーと衝突するが、この冷却チャンバーの材質は通
常ステンレスが使用されるため、鉄、ニッケル、クロム
等が亜鉛粉に混入してしまう。したがって、通常の方法
で製造される亜鉛粉には鉄が1〜3ppm、ニッケル、
クロムが1ppm程度含有されてしまうため、アルカリ
電池に無汞化で使用できるような、ガス発生が十分に低
減された亜鉛合金粉末を安定して安価に製造することが
困難であった。[0006] The impurities are mixed into the zinc alloy powder by the following route in addition to the mixing from the raw materials to be used. First, zinc alloy powder is usually produced by the atomization method. This is to dissolve zinc as a raw material, add a predetermined alloying metal, flow down the molten metal in a fine stream, and inject high-pressure gas into it. This is a method of processing into a powder. The zinc alloy powder for an alkaline battery is a product obtained by classifying the atomized zinc alloy powder to a desired particle size and then removing iron mixed from a production line by a magnetic separator. In this manufacturing method, in the step of dissolving the raw materials,
Pollution due to contamination of iron remaining in the melting furnace and contamination of iron, nickel and chromium from the material of the dross processing machine occur during dross treatment accompanying the dissolution of raw material zinc. Further, the fine molten droplets generated in the atomizing step collide with the cooling chamber. However, since the material of the cooling chamber is usually stainless steel, iron, nickel, chromium and the like are mixed in the zinc powder. Therefore, zinc powder produced by the usual method contains 1-3 ppm of iron, nickel,
Since about 1 ppm of chromium is contained, it has been difficult to stably and inexpensively produce a zinc alloy powder having sufficiently reduced gas generation, which can be used in an alkaline battery without the use of calomel.
【0007】本発明は、上述の欠点を解消すべくなされ
たもので、その目的は特定不純物がある程度混入してい
ても、合金組成の改良に加えてアトマイズ時の単位時間
当たりの亜鉛溶湯供給量とアトマイズガス供給量の比を
制御することで水素ガス発生が大幅に抑制されたアルカ
リ電池用亜鉛合金粉末を提供することにある。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned drawbacks. The object of the present invention is to improve the alloy composition and to supply the molten zinc per unit time at the time of atomization, even if specific impurities are mixed to some extent. Another object of the present invention is to provide a zinc alloy powder for an alkaline battery in which the generation of hydrogen gas is significantly suppressed by controlling the ratio of the amount of supplied hydrogen and the amount of atomized gas.
【0008】[0008]
【課題を解決するための手段】本発明者らは、この目的
に沿って鋭意研究したところ、特定の添加金属を亜鉛溶
湯に添加し、単位時間当たりの溶湯供給量とアトマイズ
ガス供給量の比を1〜5Kg/Nm3とすることで、添
加金属が効果的にガス発生を低減させる作用をすること
が判明し、亜鉛合金粉末中の不純物含有量が高い場合に
おいても水素ガス発生量が大幅に抑制されることを見い
だし本発明に到達した。すなわち、特定の組成を有する
亜鉛合金溶湯を用いて、単位時間当たりの亜鉛溶湯供給
量と噴霧に用いるガスの供給量との比を適正範囲の値に
制御しながらアトマイズすることによって、従来は使用
不可とされた不純物の多い亜鉛合金を原料として用いて
も、水素ガス発生量が抑制された亜鉛合金粉末を製造で
きることが確認された。その結果、不純物として鉄を1
ppm以上含む亜鉛合金、例えば、従来はアルカリ電池
用亜鉛合金として使用できないと考えられていた2〜5
ppmの鉄を含む亜鉛合金、あるいはそれに加えてニッ
ケルまたはクロムの少なくとも一方が1ppmを越える
量で含まれている亜鉛合金を噴霧原料として用いること
によっても、水素ガス発生量が例えば25μL/g・d
ay以下となる程度に十分に抑制された、アルカリ電池
用として好適な亜鉛合金粉末を問題なく製造できるよう
になった。Means for Solving the Problems The inventors of the present invention have conducted intensive studies for this purpose, and have found that a specific additive metal is added to a molten zinc and a ratio of a molten metal supply amount to an atomized gas supply amount per unit time. Is set to 1 to 5 kg / Nm 3 , it has been found that the added metal has an effect of effectively reducing gas generation, and even when the content of impurities in the zinc alloy powder is high, the amount of generated hydrogen gas is large. And reached the present invention. That is, by using a zinc alloy melt having a specific composition and atomizing while controlling the ratio of the supply amount of the zinc melt per unit time and the supply amount of the gas used for spraying to a value within an appropriate range, the conventional method is used. It was confirmed that a zinc alloy powder with a reduced amount of hydrogen gas generated can be produced even when a zinc alloy containing many impurities, which are considered to be impossible, is used as a raw material. As a result, iron as an impurity
ppm or more of zinc alloys, for example, 2 to 5 which were conventionally considered to be unusable as zinc alloys for alkaline batteries
The use of a zinc alloy containing 1 ppm of iron or a zinc alloy containing at least one of nickel and chromium in an amount exceeding 1 ppm in addition to the above as a raw material for spraying can also reduce the amount of hydrogen gas generated, for example, to 25 μL / g · d.
It is possible to produce a zinc alloy powder sufficiently suppressed to ay or less and suitable for an alkaline battery without any problem.
【0009】すなわち、本発明は第1に、ビスマスを
0.001〜0.1重量%、インジウムを0.001〜
0.1重量%含有し、残部が亜鉛および不可避不純物か
らなることを特徴とするアルカリ電池用亜鉛合金粉末;
第2に、アルミニウムを0.001〜0.1重量%含有
することを特徴とする前記第1記載のアルカリ電池用亜
鉛合金粉末;第3に、マグネシウムを0.001〜0.
1重量%含有することを特徴とする前記第1または第2
記載のアルカリ電池用亜鉛合金粉末;第4に、周期表の
13(IIIB)族元素を0.001〜0.1重量%含有する
ことを特徴とする前記第1〜3のいずれかに記載のアル
カリ電池用亜鉛合金粉末;第5に、前記13(IIIB)族元
素がイットリウムまたはランタンである前記第4に記載
のアルカリ電池用亜鉛合金粉末;第6に、2〜5ppm
の鉄または1ppmを越える量のニッケルもしくはクロ
ムの少なくとも一方または前記鉄とニッケルもしくはク
ロムの両方を含む前記第1〜5のいずれかに記載のアル
カリ電池用亜鉛合金粉末;第7に、ガス発生量が25μ
L/(g・day)以下である前記第1〜6のいずれか
に記載のアルカリ電池用亜鉛合金粉末;第8に、ビスマ
スを0.001〜0.1重量%、インジウムを0.00
1〜0.1重量%含み、残部が亜鉛および不可避不純物
からなる亜鉛合金の溶湯をアトマイズ法で霧化して亜鉛
合金粉末とする際、上記亜鉛合金溶湯の供給量とアトマ
イズガス供給量との比が、1〜5kg/Nm3であるこ
とを特徴とするアルカリ電池用亜鉛合金粉末の製造方
法;第9に、前記亜鉛合金がビスマス、インジウムの他
にアルミニウムの0.001〜0.1重量%を含む前記
第8記載の製造方法;第10に、前記亜鉛合金がビスマ
ス、インジウムの他にマグネシウムの0.001〜0.
1重量%を含む前記第8または9記載のアルカリ電池用
亜鉛合金粉末の製造方法;第11に、前記亜鉛合金がビ
スマス、インジウムの他に周期表の13(IIIB)族元素の
0.001〜0.1重量%を含む前記第8ないし10の
いずれかに記載のアルカリ電池用亜鉛合金粉末の製造方
法を提供するものである。That is, the present invention firstly provides 0.001 to 0.1% by weight of bismuth and 0.001% to indium.
A zinc alloy powder for an alkaline battery, comprising 0.1% by weight, with the balance being zinc and unavoidable impurities;
Second, the zinc alloy powder for an alkaline battery according to the first aspect, wherein the zinc alloy powder contains 0.001 to 0.1% by weight of aluminum;
1% by weight or 1% by weight.
4. The zinc alloy powder for an alkaline battery according to any one of the first to third aspects, wherein the zinc alloy powder further comprises 0.001 to 0.1% by weight of a Group 13 (IIIB) element of the periodic table. Fifth, the zinc alloy powder for an alkaline battery according to the fourth aspect, wherein the group 13 (IIIB) element is yttrium or lanthanum;
7. The zinc alloy powder for an alkaline battery according to any one of the first to fifth aspects, wherein the zinc alloy powder contains at least one of iron or nickel or chromium in an amount exceeding 1 ppm, or both iron and nickel or chromium; Is 25μ
The zinc alloy powder for an alkaline battery according to any one of the first to sixth aspects, wherein L / (g · day) or less; eighthly, 0.001 to 0.1% by weight of bismuth and 0.00% of indium.
When atomizing a molten zinc alloy containing 1 to 0.1% by weight, with the balance being zinc and unavoidable impurities, by atomizing into a zinc alloy powder, the ratio between the supply amount of the molten zinc alloy and the supplied amount of the atomized gas. There, 1-5 kg / Nm 3 manufacturing method of the zinc alloy powder for alkaline batteries, which is a; ninth, the zinc alloy is of bismuth, in addition to 0.001 wt% aluminum indium Tenth, the tenth aspect is that the zinc alloy contains 0.001 to 0. 0 of magnesium in addition to bismuth and indium.
The method for producing a zinc alloy powder for an alkaline battery according to the eighth or ninth aspect containing 1% by weight; eleventh, the zinc alloy contains 0.001 to 13 (IIIB) group elements of the periodic table in addition to bismuth and indium. 11. A method for producing a zinc alloy powder for an alkaline battery according to any one of the eighth to tenth aspects, wherein the zinc alloy powder contains 0.1% by weight.
【0010】[0010]
【発明の実施の形態】本発明のアルカリ電池用亜鉛合金
粉末製造における各合金元素の添加の効果は以下の通り
である。亜鉛とKOH水溶液に代表されるアルカリ性電
解液との反応による水素ガス発生は、亜鉛粒子表面に存
在する局部電池上で電解液中の水分が次式の反応のよう
に電気分解されることにより生じるものとされている。 2H2O + 2e− → 2OH− + H2↑DESCRIPTION OF THE PREFERRED EMBODIMENTS The effects of the addition of each alloy element in the production of a zinc alloy powder for an alkaline battery according to the present invention are as follows. Hydrogen gas generation by the reaction between zinc and an alkaline electrolyte represented by a KOH aqueous solution is caused by electrolysis of water in the electrolyte on a local battery existing on the surface of zinc particles as in the following reaction. It is assumed. 2H 2 O + 2e - → 2OH - + H 2 ↑
【0011】この局部電池は亜鉛と亜鉛中の不純物間の
電位差により生じるが、鉄、ニッケル、クロム等の水素
過電圧が低い元素と局部電池を形成した場合、この不純
物元素上でガス発生が生じ、これら不純物含有量が多い
ほどガス発生量は大となる。そこで、これら不純物より
貴な電位を有し、水素過電圧の高い元素を亜鉛に添加す
れば、不純物が原因によるガス発生を抑制することが可
能となる。このガス発生を抑制するためにビスマス、イ
ンジウムを添加するが、これらの元素は比較的貴な電位
を有し、かつそれ自体の水素過電圧が高いため、亜鉛に
添加することで上述したように亜鉛の水素過電圧を高
め、ガス発生を抑制する効果を発揮しているものと推測
される。This local battery is generated by a potential difference between zinc and impurities in zinc. When a local battery is formed with an element having a low hydrogen overvoltage such as iron, nickel, and chromium, gas is generated on the impurity element, The greater the content of these impurities, the greater the amount of gas generated. Therefore, if an element having a higher potential than the impurities and having a higher hydrogen overvoltage is added to zinc, gas generation due to the impurities can be suppressed. Bismuth and indium are added to suppress this gas generation, but since these elements have a relatively noble potential and a high hydrogen overpotential of themselves, zinc is added to zinc as described above. It is presumed that the hydrogen overvoltage is increased and the effect of suppressing gas generation is exhibited.
【0012】また、アルミニウム,マグネシウムおよび
13(IIIB)族元素は、それ自体は水素過電圧が低いの
で、ガス発生の抑制は上述のビスマスおよびインジウム
とは異なる作用によるものと推測される。ここで、水素
ガス発生の原因となる局部電池は、上述の不純物の他に
亜鉛の酸化物によっても形成され、それによりガスが発
生するとされており、不純物含有量を下げる他に、酸化
物の生成を抑制することでガス発生の低減が可能とな
る。Further, since aluminum, magnesium and group 13 (IIIB) elements themselves have a low hydrogen overpotential, it is presumed that suppression of gas generation is caused by a different effect from bismuth and indium described above. Here, the local battery that causes hydrogen gas generation is also formed of zinc oxide in addition to the above-described impurities, which is said to generate gas. By suppressing generation, gas generation can be reduced.
【0013】この亜鉛の酸化物は、主に亜鉛溶湯とアト
マイズガスとの反応により生じる。そこで、アトマイズ
ガスを不活性ガスとし、酸化物の形成を抑制する方法も
考えられるが、不活性ガスをアトマイズガスとした場
合、水素ガス発生は低減できるものの、放電性能の劣化
が生じる。これは不活性ガスを用いてアトマイズした場
合、亜鉛の粒子形状は微少融滴が凝固する過程で、表面
張力で球状となるが、このように球状粒子になると、電
池に組み込むために亜鉛合金粉末をゲル状に加工した場
合、亜鉛粒子間および亜鉛粒子と集電棒との接点が少な
くなり、電池の内部抵抗を増大させるため放電性能が劣
化するのであると考えられている。そこで、アトマイズ
ガスとしては、酸素を含有するガスを用い、亜鉛溶湯が
微少融滴に分散されると同時に表面を酸化させ、酸化皮
膜の形成により形状を保持したまま、この融滴を凝固さ
せ、針状、涙滴状等の不規則形状にする方法が通常用い
られている。このため、亜鉛粒子には酸化物が存在する
こととなる。そこで、亜鉛の酸化物形成を抑制するため
に亜鉛よりも酸素と結合し易い元素を添加することによ
り、亜鉛粒子中の酸素をこれら添加元素に結合させるこ
とで亜鉛の酸化物の形成が抑制され、結果的に亜鉛の水
素過電圧を高め、水素ガス発生が低減されることが期待
される。アルミニウム、マグネシウムおよび13(IIIB)
族元素は、亜鉛よりも酸素と結合し易いのでアトマイズ
時に生じる亜鉛酸化物の形成を効果的に抑制し、このた
め、水素ガス発生が抑制されるものと推測される。The zinc oxide is mainly generated by the reaction between the molten zinc and the atomizing gas. Therefore, a method of suppressing the formation of oxides by using an atomizing gas as an inert gas is conceivable. However, when the atomizing gas is used as an inert gas, the generation of hydrogen gas can be reduced, but the discharge performance deteriorates. This is because when atomized with an inert gas, the zinc particle shape becomes spherical due to surface tension in the process of solidification of the fine droplets. It is believed that when the is processed into a gel, the number of contacts between zinc particles and between the zinc particles and the current collecting rod is reduced, and the internal resistance of the battery is increased, so that the discharge performance is deteriorated. Therefore, as an atomizing gas, a gas containing oxygen is used, and the surface of the zinc melt is oxidized at the same time as the molten zinc is dispersed in the fine molten droplets, and while maintaining the shape by forming an oxide film, the molten droplets are solidified. A method of forming an irregular shape such as a needle shape or a teardrop shape is generally used. Therefore, an oxide is present in the zinc particles. Therefore, by adding an element that is more easily bonded to oxygen than zinc in order to suppress the formation of zinc oxide, the formation of zinc oxide is suppressed by bonding oxygen in the zinc particles to these added elements. As a result, it is expected that the hydrogen overvoltage of zinc is increased and the generation of hydrogen gas is reduced. Aluminum, magnesium and 13 (IIIB)
It is presumed that the group-group element is more likely to bond with oxygen than zinc, and thus effectively suppresses the formation of zinc oxide generated during atomization, thereby suppressing the generation of hydrogen gas.
【0014】しかし、上述の作用を有する元素を亜鉛に
添加しても、その効果が十分に発揮されない場合のある
ことが判明した。そこで本発明者らは、アトマイズ工程
での制御条件を詳細に検討したところ、溶湯供給量とア
トマイズガス供給量の比を所定の値にすることで、添加
金属の作用をより効果的に発揮させられることが分かっ
た。その理由は現在まだ明確となっていないが、おおよ
そ次のように推測される。溶湯供給量とアトマイズガス
供給量の比が小さい場合は、融滴の冷却速度が大きく、
急冷されるため、ガス発生抑制のために添加した元素が
粒子全体に均一に分散した状態で冷却される。これに対
して溶湯供給量とアトマイズガス供給量の比が大きい場
合は冷却速度が比較的小さくなるため、Bi、Inなど
亜鉛より凝固点の低い元素は粒界や粒子表面に染み出
し、粒子表面近傍に濃縮される。また、Al、13(III
B)族元素などアトマイズガス中の酸素と結合し易い元素
は、冷却速度が小さく、融滴の温度が高い場合は、酸化
反応の進行により、粒子表面近傍に濃縮される。なお、
これら3価の価数を有する元素は亜鉛粒子表面に生成す
る酸化亜鉛粒子内に固溶することで酸化亜鉛の導電性を
増し、これにより亜鉛粒子表面に生成する酸化亜鉛の水
素過電圧を高める事ができる。これらの事により、各添
加金属が亜鉛粒子表面に濃縮されることで亜鉛粒子表面
の水素過電圧を高め、同じ添加量においても、前記比の
値が適正範囲内にない場合に比し、鉄、ニッケル、クロ
ムなどの不純物の悪影響を弱めることが可能と考えられ
る。なお、亜鉛溶湯供給量とアトマイズガス供給量の比
を1〜5kg/Nm3としたのは、lkg/Nm3未満で
は上述の添加元素の表面濃縮が十分に行われないため、
ガス発生抑制効果が小さくなるためであり、5kg/N
m3を超えると、添加元素は表面近傍へ濃縮されるもの
の、微少融滴への分散が十分に行われないため、アルカ
リ電池用亜鉛合金粉に使用されるような所定の粒度が得
られなくなるからである。以下、本発明を実施例により
詳細に説明する。しかし、本発明の範囲は以下の実施例
により制限されるものではない。However, it has been found that even if an element having the above-mentioned action is added to zinc, the effect may not be sufficiently exhibited. Then, the present inventors examined the control conditions in the atomizing process in detail, and found that the ratio of the molten metal supply amount and the atomized gas supply amount was set to a predetermined value, so that the effect of the added metal was more effectively exerted. I knew it could be done. The reason for this has not been clarified yet, but is presumed to be roughly as follows. When the ratio between the supply amount of the molten metal and the supply amount of the atomizing gas is small, the cooling rate of the droplet is high,
Because of the rapid cooling, the element added for suppressing gas generation is cooled while being uniformly dispersed throughout the particles. On the other hand, when the ratio between the supply amount of the molten metal and the supply amount of the atomizing gas is large, the cooling rate is relatively low. Is concentrated. Al, 13 (III
When the cooling rate is low and the temperature of the molten droplet is high, elements that easily bond to oxygen in the atomizing gas such as group B) elements are concentrated near the particle surface due to the progress of the oxidation reaction. In addition,
These trivalent elements increase the conductivity of zinc oxide by forming a solid solution in zinc oxide particles formed on the surface of zinc particles, thereby increasing the hydrogen overvoltage of zinc oxide generated on the surface of zinc particles. Can be. Due to these facts, each added metal is concentrated on the surface of the zinc particles to increase the hydrogen overvoltage on the surface of the zinc particles.Even with the same amount of addition, compared to the case where the value of the ratio is not within an appropriate range, iron, It is considered possible to reduce the adverse effects of impurities such as nickel and chromium. In addition, the reason why the ratio of the supply amount of the molten zinc to the supply amount of the atomizing gas is set to 1 to 5 kg / Nm 3 is that if the amount is less than 1 kg / Nm 3 , the surface concentration of the above-described additional element is not sufficiently performed.
5 kg / N
Beyond m 3, although the additive element is concentrated to near the surface, the dispersion of the fine Torushizuku is not sufficiently, can not be obtained a predetermined particle size as used in the zinc alloy powder for alkaline batteries Because. Hereinafter, the present invention will be described in detail with reference to examples. However, the scope of the present invention is not limited by the following examples.
【0015】[0015]
【実施例1〜15】純度99.995%以上の亜鉛を原
料とし、約500℃で溶融させ、これに表1に示す所定
量のアルミニウム、ビスマス、インジウム、マグネシウ
ムおよび13(IIIB)族元素としてイットリウム、ランタ
ンを添加し、亜鉛合金溶湯を作成した。この溶湯をセラ
ミックス製のノズルを用いて細流状に滴下させ、これに
圧縮空気もしくは酸素を付加した窒素ガスを噴射させ、
亜鉛合金粉末を得た。得られた亜鉛合金粉末を#35〜
200メッシュの粒度に分級した後、鉄の含有量および
ガス発生量を求めた。ガス発生量の測定は、亜鉛合金粉
末を所定量投入し、40%KOH溶液を添加後、流動パ
ラフィンを満たしてシリコーンゴム栓で封じた試験管を
60℃の恒温槽に保持し、所定の時間経過後のメスピぺ
ツトの目盛を読むことでガス発生速度を求めた。表1に
示されているように鉄の含有量が2〜5ppm程度であ
っても、特定の組成を有し、特定の溶湯−ガス供給速度
比(単位時間当たりの溶湯供給量対単位時間当たりのア
トマイズガス供給量の比)とした実施例1〜15はいず
れもガス発生量が許容限度である25μL/(g・da
y)よりも少ない。Examples 1 to 15 Zinc having a purity of 99.995% or more was melted at about 500 ° C., and a predetermined amount of aluminum, bismuth, indium, magnesium and a 13 (IIIB) group element shown in Table 1 were added thereto. Yttrium and lanthanum were added to prepare a molten zinc alloy. Using a ceramic nozzle, the molten metal is dropped in a rivulet form, and compressed air or nitrogen gas to which oxygen has been added is jetted onto the molten metal.
A zinc alloy powder was obtained. The obtained zinc alloy powder was # 35-
After classifying to a particle size of 200 mesh, the iron content and gas generation were determined. Measurement of gas generation amount is as follows: After a predetermined amount of zinc alloy powder is added, a 40% KOH solution is added, a test tube filled with liquid paraffin and sealed with a silicone rubber stopper is kept in a thermostat at 60 ° C. for a predetermined time. The gas generation rate was determined by reading the scale of the massage after the passage. As shown in Table 1, even when the iron content is about 2 to 5 ppm, it has a specific composition and a specific molten metal-gas supply rate ratio (the amount of molten metal supplied per unit time per unit time). In all of Examples 1 to 15 in which the ratio of the amount of atomized gas supplied was 25 μL / (g · da) where the amount of generated gas was an allowable limit.
less than y).
【0016】[0016]
【表1】 [Table 1]
【0017】[0017]
【比較例1〜8】前記実施例に対して、溶湯−ガス供給
速度比のみを変化させた比較例1〜3ではいずれもガス
発生量が許容限度を上回っている。比較例4〜8では溶
湯−ガス供給速度比は範囲内であるが、添加成分がいず
れも範囲外のものであり、いずれもガス発生量が許容限
度を上回っている。Comparative Examples 1 to 8 In Comparative Examples 1 to 3, in which only the molten metal-gas supply speed ratio was changed, the gas generation amount exceeded the allowable limit. In Comparative Examples 4 to 8, the molten metal-gas supply rate ratio was within the range, but the added components were all outside the range, and the gas generation amount exceeded the allowable limit in all cases.
【0018】[0018]
【発明の効果】以上説明したように、本発明の方法によ
れば、亜鉛粉の代表的な不純物である鉄の含有量を極微
量に低減することなく、特定の合金組成範囲にすると共
に、アトマイズ時の溶湯−ガス供給速度比を特定の範囲
とすることで、水素ガスの発生を抑制して電池特性を向
上させ得るアルカリ電池用亜鉛合金粉末が容易に得られ
る。As described above, according to the method of the present invention, the content of iron, which is a typical impurity of zinc powder, is reduced to a specific alloy composition range without being reduced to an extremely small amount. By setting the molten metal-gas supply rate ratio at the time of atomization to a specific range, a zinc alloy powder for an alkaline battery which can suppress generation of hydrogen gas and improve battery characteristics can be easily obtained.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 張替 彦一 東京都千代田区丸の内1丁目8番2号 同 和鉱業株式会社内 (72)発明者 小山 泰幸 東京都千代田区丸の内1丁目8番2号 同 和鉱業株式会社内 (72)発明者 佐藤 文洋 東京都千代田区丸の内1丁目8番2号 同 和鉱業株式会社内 Fターム(参考) 4K017 AA04 BA01 BB01 BB03 BB04 BB06 BB12 BB18 DA09 EB07 FA09 4K018 BA10 BD10 KA38 5H050 AA15 BA04 CA05 CB13 DA09 EA02 EA03 EA07 FA17 HA00 HA01 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Hikoichi Harikai 1-8-2 Marunouchi, Chiyoda-ku, Tokyo Dowa Mining Co., Ltd. (72) Inventor Yasuyuki Koyama 1-8-2 Marunouchi, Chiyoda-ku, Tokyo No. Dowa Mining Co., Ltd. (72) Inventor Fumihiro Sato 1-8-2 Marunouchi, Chiyoda-ku, Tokyo F-term (reference) 4K017 AA04 BA01 BB01 BB03 BB04 BB06 BB12 BB18 DA09 EB07 FA09 4K018 BA10 BD10 KA38 5H050 AA15 BA04 CA05 CB13 DA09 EA02 EA03 EA07 FA17 HA00 HA01
Claims (11)
インジウムを0.001〜0.1重量%含有し、残部が
亜鉛および不可避不純物からなることを特徴とするアル
カリ電池用亜鉛合金粉末。1. Bismuth in an amount of 0.001 to 0.1% by weight,
A zinc alloy powder for an alkaline battery, comprising 0.001 to 0.1% by weight of indium, with the balance being zinc and unavoidable impurities.
%含有することを特徴とする請求項1記載のアルカリ電
池用亜鉛合金粉末。2. The zinc alloy powder for an alkaline battery according to claim 1, comprising 0.001 to 0.1% by weight of aluminum.
%含有することを特徴とする請求項1または2記載のア
ルカリ電池用亜鉛合金粉末。3. The zinc alloy powder for an alkaline battery according to claim 1, comprising 0.001 to 0.1% by weight of magnesium.
〜0.1重量%含有することを特徴とする請求項1〜3
のいずれかに記載のアルカリ電池用亜鉛合金粉末。4. An element of group 13 (IIIB) of the periodic table having a content of 0.001
4 to 0.1% by weight.
The zinc alloy powder for an alkaline battery according to any one of the above.
たはランタンである請求項4に記載のアルカリ電池用亜
鉛合金粉末。5. The zinc alloy powder for an alkaline battery according to claim 4, wherein the group 13 (IIIB) element is yttrium or lanthanum.
る量のニッケルもしくはクロムの少なくとも一方または
前記鉄とニッケルもしくはクロムの両方を含む請求項1
〜5のいずれかに記載のアルカリ電池用亜鉛合金粉末。6. The method according to claim 1, which comprises from 2 to 5 ppm of iron or at least one of nickel and chromium in an amount exceeding 1 ppm or both said iron and nickel or chromium.
6. The zinc alloy powder for an alkaline battery according to any one of items 1 to 5.
以下である請求項1〜6のいずれかに記載のアルカリ電
池用亜鉛合金粉末。7. The gas generation amount is 25 μL / (g · day).
The zinc alloy powder for an alkaline battery according to any one of claims 1 to 6, which is:
インジウムを0.001〜0.1重量%含み、残部が亜
鉛および不可避不純物からなる亜鉛合金の溶湯をアトマ
イズ法で霧化して亜鉛合金粉末とする際、上記亜鉛合金
溶湯の供給量とアトマイズガス供給量との比が、1〜5
kg/Nm3であることを特徴とするアルカリ電池用亜
鉛合金粉末の製造方法。8. Bismuth in an amount of 0.001 to 0.1% by weight,
When the molten zinc alloy containing 0.001 to 0.1% by weight of indium and the remainder consisting of zinc and unavoidable impurities is atomized by an atomizing method into a zinc alloy powder, the supply amount of the molten zinc alloy and the supply of the atomized gas The ratio with the amount is 1-5
kg / Nm 3. A method for producing a zinc alloy powder for an alkaline battery.
他にアルミニウムの0.001〜0.1重量%を含む請
求項8記載の製造方法。9. The method according to claim 8, wherein the zinc alloy contains 0.001 to 0.1% by weight of aluminum in addition to bismuth and indium.
の他にマグネシウムの0.001〜0.1重量%を含む
請求項8または9記載のアルカリ電池用亜鉛合金粉末の
製造方法。10. The method for producing a zinc alloy powder for an alkaline battery according to claim 8, wherein the zinc alloy contains 0.001 to 0.1% by weight of magnesium in addition to bismuth and indium.
の他に周期表の13(IIIB)族元素の0.001〜0.1
重量%を含む請求項8ないし10のいずれかに記載のア
ルカリ電池用亜鉛合金粉末の製造方法。11. The zinc alloy contains 0.001 to 0.1 of a Group 13 (IIIB) element of the periodic table in addition to bismuth and indium.
The method for producing a zinc alloy powder for an alkaline battery according to any one of claims 8 to 10, wherein the method further comprises a percentage by weight.
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|---|---|---|---|
| JP2000090271A JP4852713B2 (en) | 2000-03-29 | 2000-03-29 | Zinc alloy powder for alkaline batteries and method for producing the same |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000090271A JP4852713B2 (en) | 2000-03-29 | 2000-03-29 | Zinc alloy powder for alkaline batteries and method for producing the same |
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| Publication Number | Publication Date |
|---|---|
| JP2001283842A true JP2001283842A (en) | 2001-10-12 |
| JP4852713B2 JP4852713B2 (en) | 2012-01-11 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006045470A1 (en) * | 2004-10-20 | 2006-05-04 | Umicore | Alloyed zinc powders for alkaline batteries with high pyknometer density |
| JP2007173254A (en) * | 2007-02-23 | 2007-07-05 | Hitachi Maxell Ltd | Alkaline battery |
| WO2007129285A2 (en) | 2006-05-09 | 2007-11-15 | The Gillette Company | Battery anodes |
| US7510801B2 (en) | 2002-07-12 | 2009-03-31 | Hitachi Maxell, Ltd. | Alkaline battery and method for producing the same |
| CN111146431A (en) * | 2020-02-11 | 2020-05-12 | 河南创力新能源科技股份有限公司 | Iron-nickel battery cathode composite material and preparation method thereof |
| CN111146408A (en) * | 2020-02-11 | 2020-05-12 | 河南创力新能源科技股份有限公司 | Preparation method of iron-nickel battery cathode |
| CN114597388A (en) * | 2022-03-16 | 2022-06-07 | 宁波双鹿新能源科技有限公司 | Zinc material special for battery and production process thereof |
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| JPH04289661A (en) * | 1991-03-18 | 1992-10-14 | Mitsui Mining & Smelting Co Ltd | Zinc alloy powder for alkaline battery and manufacture thereof |
| JPH05299083A (en) * | 1992-04-24 | 1993-11-12 | Mitsui Mining & Smelting Co Ltd | Zinc alloy powder for alkaline battery and manufacture thereof |
| JPH09259877A (en) * | 1996-03-19 | 1997-10-03 | Fuji Elelctrochem Co Ltd | Negative electrode zinc-based alloy for alkaline batteries |
| JPH10172555A (en) * | 1996-12-17 | 1998-06-26 | Toshiba Battery Co Ltd | Zinc alkaline battery |
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| JPH05299083A (en) * | 1992-04-24 | 1993-11-12 | Mitsui Mining & Smelting Co Ltd | Zinc alloy powder for alkaline battery and manufacture thereof |
| JPH09259877A (en) * | 1996-03-19 | 1997-10-03 | Fuji Elelctrochem Co Ltd | Negative electrode zinc-based alloy for alkaline batteries |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7510801B2 (en) | 2002-07-12 | 2009-03-31 | Hitachi Maxell, Ltd. | Alkaline battery and method for producing the same |
| US7767336B2 (en) | 2002-07-12 | 2010-08-03 | Hitachi Maxell, Ltd. | Alkaline battery and method for producing the same |
| WO2006045470A1 (en) * | 2004-10-20 | 2006-05-04 | Umicore | Alloyed zinc powders for alkaline batteries with high pyknometer density |
| WO2007129285A2 (en) | 2006-05-09 | 2007-11-15 | The Gillette Company | Battery anodes |
| WO2007129285A3 (en) * | 2006-05-09 | 2008-01-24 | Gillette Co | Battery anodes |
| JP2007173254A (en) * | 2007-02-23 | 2007-07-05 | Hitachi Maxell Ltd | Alkaline battery |
| CN111146431A (en) * | 2020-02-11 | 2020-05-12 | 河南创力新能源科技股份有限公司 | Iron-nickel battery cathode composite material and preparation method thereof |
| CN111146408A (en) * | 2020-02-11 | 2020-05-12 | 河南创力新能源科技股份有限公司 | Preparation method of iron-nickel battery cathode |
| CN114597388A (en) * | 2022-03-16 | 2022-06-07 | 宁波双鹿新能源科技有限公司 | Zinc material special for battery and production process thereof |
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|---|---|
| JP4852713B2 (en) | 2012-01-11 |
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