JP2584035B2 - Method for producing zinc oxide whiskers - Google Patents
Method for producing zinc oxide whiskersInfo
- Publication number
- JP2584035B2 JP2584035B2 JP63328271A JP32827188A JP2584035B2 JP 2584035 B2 JP2584035 B2 JP 2584035B2 JP 63328271 A JP63328271 A JP 63328271A JP 32827188 A JP32827188 A JP 32827188A JP 2584035 B2 JP2584035 B2 JP 2584035B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- powder
- whisker
- zinc oxide
- container
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 title description 75
- 239000011787 zinc oxide Substances 0.000 title description 36
- 238000004519 manufacturing process Methods 0.000 title description 18
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 53
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 12
- 239000001301 oxygen Substances 0.000 claims description 12
- 229910052760 oxygen Inorganic materials 0.000 claims description 12
- 239000000843 powder Substances 0.000 description 47
- 238000000034 method Methods 0.000 description 34
- 229910052725 zinc Inorganic materials 0.000 description 23
- 239000011701 zinc Substances 0.000 description 23
- 239000013078 crystal Substances 0.000 description 21
- 229910052751 metal Inorganic materials 0.000 description 21
- 239000002184 metal Substances 0.000 description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 239000002245 particle Substances 0.000 description 19
- 238000007789 sealing Methods 0.000 description 16
- 238000010304 firing Methods 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 230000012010 growth Effects 0.000 description 10
- 241001455273 Tetrapoda Species 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 230000032683 aging Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 238000000635 electron micrograph Methods 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 239000000779 smoke Substances 0.000 description 7
- 238000002441 X-ray diffraction Methods 0.000 description 6
- 230000007547 defect Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000002003 electron diffraction Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000005507 spraying Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 229910052573 porcelain Inorganic materials 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000001479 atomic absorption spectroscopy Methods 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000010303 mechanochemical reaction Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 230000034655 secondary growth Effects 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- 229910001297 Zn alloy Inorganic materials 0.000 description 1
- OLBVUFHMDRJKTK-UHFFFAOYSA-N [N].[O] Chemical compound [N].[O] OLBVUFHMDRJKTK-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 238000001241 arc-discharge method Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000002431 foraging effect Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
- -1 that is Substances 0.000 description 1
- 238000007751 thermal spraying Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 238000000927 vapour-phase epitaxy Methods 0.000 description 1
- 150000003752 zinc compounds Chemical class 0.000 description 1
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、巨大なテトラポッド状構造を有する酸化亜
鉛ウィスカー集合体の製造方法に関する。Description: TECHNICAL FIELD The present invention relates to a method for producing a zinc oxide whisker aggregate having a huge tetrapod-like structure.
従来の技術 現在、一般的工業材料として使用される酸化亜鉛はい
わゆるフランス法によるものが多く、粒子の大きさ、特
に形状がまちまちの団魂状粒子の集合体である。又、細
く短い針状結晶粒子に高収率で形成させる方法(例えば
特公昭60−5529号公報)があるが、これは上記フランス
法の改良法で、加熱亜鉛蒸気を炉外に導き急速に冷却す
るものであり、このため巨大結晶体は生成せず、微小寸
法(長さが0.1〜15μm)の針状結晶となる。2. Description of the Related Art At present, zinc oxide used as a general industrial material is often based on the so-called French method, and is an aggregate of gang-like particles having various particle sizes, especially shapes. There is also a method of forming fine and short needle-like crystal grains with a high yield (for example, Japanese Patent Publication No. Sho 60-5529). This method is an improvement of the above-mentioned French method. This is to cool, so that a giant crystal is not formed, and it becomes a needle-like crystal having a minute dimension (length: 0.1 to 15 μm).
この様な寸法の針状結晶体は現在市販されている各種
工業用ウィスカーと比較すると寸法面で約2桁小さい。
このため、前記ウィスカーの共通的特長である金属、セ
ラミック、樹脂等への補強効果は前記団魂状酸化亜鉛の
水準と大差なく、ウィスカー的な顕著な効果は認められ
ない。繊維形状の単結晶性であるウィスカーは同材質の
団魂状物質よりは格段と機械的強度が大でこれを他の物
質中に混入して高い機械的強度を得るための強化物質と
して注目されており、現在では、金属、金属酸化物、金
属炭化物、金属窒化物等の工業用ウィスカーが市販され
ている。又酸化亜鉛においても長さがmm桁のウィスカー
の例(特開昭50−5597号公報)等があるが、これは単純
針状体のもので、わざわざ亜鉛の合金を用いるため、結
晶中に不純物を含んだり、成長時に原料設置前から離れ
た位置に基板を設けことを必要としたり、低収率であっ
たり、複雑な装置、操作で長時間を要する等の実験室的
検討に過ぎないものが多い。Needle-like crystals of such dimensions are approximately two orders of magnitude smaller in size in comparison with various commercially available industrial whiskers.
For this reason, the reinforcing effect on the metal, ceramic, resin, and the like, which is a common feature of the whiskers, is not much different from the level of the gang-like zinc oxide, and no remarkable whisker effect is observed. Whisker, which is a fiber-shaped single crystal, has much higher mechanical strength than the same material of the same material, and is attracting attention as a reinforcing material to obtain high mechanical strength by mixing it with other materials. At present, industrial whiskers of metals, metal oxides, metal carbides, metal nitrides and the like are commercially available. As for zinc oxide, there is an example of a whisker having a length of mm order (Japanese Patent Application Laid-Open No. 50-5597). This is a simple needle-shaped body, and a zinc alloy is used. It is only a laboratory study that contains impurities, requires a substrate to be provided at a position away from the source material during growth, low yield, complicated equipment, long operation time, etc. There are many things.
発明が解決しようとする課題 本発明は工業用ウィスター級の寸法性或はこれら以上
の寸法を有する酸化亜鉛の巨大結晶体の集合体を得る製
造法を提供することを目的とする。また、本発明は巨大
テトラポッド状構造の酸化亜鉛ウィスカー集合体の新規
な製造方法を提供するものである。DISCLOSURE OF THE INVENTION An object of the present invention is to provide a method for obtaining an aggregate of large crystals of zinc oxide having dimensional properties of industrial Wistar grade or larger. The present invention also provides a novel method for producing a zinc oxide whisker aggregate having a giant tetrapod-like structure.
課題を解決するための手段 本発明による酸化亜鉛ウィスカーの製造方法は、表面
に酸化皮膜を有する亜鉛粉末を酸素を含む雰囲気下で加
熱処理して酸化亜鉛を生成させることを特徴とする。前
記フランス法の改良法や単純針状結晶体製造方法等の如
く、原料設置場所とウィスカー生成、成長箇所が分離区
分されているのが従来気相法ウィスカー製造方法の特徴
でもある。しかるに本発明では一面が開口した容器を用
いる。この容器の開口面に対応する面を底面とし、この
底面上に上記亜鉛粉末を設置して、この容器ごと予め加
熱された炉内に設置して空気など酸素を含む雰囲気下で
加熱、酸化処理を行うことにより、従来のものとは全く
かけ離れた新規な巨大テトラポッド状酸化亜鉛ウィスカ
ー重合体を製造できるし、生成したウィスカーはこの容
器内の上層部に堆積して製造される特徴を有する。又上
記容器のウィスカー堆積層より下層部には、副生する団
魂状酸化亜鉛層がウィスカー層と分離して堆積する特徴
をも有する。Means for Solving the Problems A method for producing a zinc oxide whisker according to the present invention is characterized in that a zinc powder having an oxide film on its surface is subjected to a heat treatment in an atmosphere containing oxygen to generate zinc oxide. It is a feature of the conventional vapor-phase whisker manufacturing method that the place where the raw material is placed and the whisker generation and growth sites are separated and divided, as in the above-mentioned French method and the method for manufacturing a simple needle crystal. In the present invention, however, a container having an open surface is used. The surface corresponding to the opening surface of this container is defined as a bottom surface, and the zinc powder is placed on the bottom surface, and the container is placed in a preheated furnace and heated and oxidized in an atmosphere containing oxygen such as air. By carrying out the above, a novel giant tetrapod-like zinc oxide whisker polymer which is completely different from the conventional one can be produced, and the produced whiskers are characterized in that they are produced by being deposited on the upper layer in this container. In addition, in the lower part of the whisker deposition layer of the above-mentioned container, a gang-like zinc oxide layer as a by-product is characterized in that it is deposited separately from the whisker layer.
又、ここにおいて、亜鉛粉末は容器の底面に層状に散
布するのが望ましいし、原材投入方法も、予め、上記容
器を炉内で加熱させた後に亜鉛粉末を容器底部に散布す
る方法も可能である。In this case, it is desirable that the zinc powder is sprayed in a layer on the bottom of the container, and the raw material charging method is also possible, in which the container is heated in advance in a furnace and then the zinc powder is sprayed on the container bottom. It is.
又、原料亜鉛粉末は表面に酸化皮膜を形成させたもの
が必須であり、酸化皮膜の形成は粉末製造時に達成され
ることが多く、これには溶融粉末を経る方法、団体状の
ままの粉砕による方法等があるが、前者は一部やや多孔
質であるが厚膜化し易く、後者はち密で薄い皮膜となる
ことが多い。In addition, it is essential that the raw material zinc powder has an oxide film formed on the surface, and the formation of the oxide film is often achieved at the time of powder production. Although the former is partially porous, the former tends to be thicker, and the latter often has a denser and thinner film.
又、亜鉛粉末に酸化皮膜を形成したり、皮膜厚を増大
させたりする好ましい方法としては、後述のように亜鉛
粉末を水と共存下で擂潰し、熟成させる方法がある。Further, as a preferable method for forming an oxide film on the zinc powder or increasing the film thickness, there is a method in which the zinc powder is crushed in the presence of water and matured as described later.
作用 本発明の方法によって得られる酸化亜鉛ウィスカー
は、中心の核部とこの核部から異なる4軸方向に伸びた
針状結晶部からなり、前記針状結晶部の基部の径が0.7
〜14μmであり、前記針状結晶部の基部から先端までの
長さが3〜200μmである。又針状結晶部が3軸或は2
軸のものも多少混入するが、これらは、成長中或は後に
他のウィスカーと接触して、その一部が折損したり、成
長が停止した結果である。又この成長中の接触により完
全なテトラポッド形の一部に他のテトラポッドが付着し
たものも多少みられる。他の形状即ち板状晶が針状態に
付着することもあるが、本発明を製造方法によればテト
ラポッド状のものが主体となる。The zinc oxide whisker obtained by the method of the present invention comprises a central nucleus and needle-like crystal parts extending in four different directions from this core, and the diameter of the base of the needle-like crystal part is 0.7 mm.
針 14 μm, and the length from the base to the tip of the needle-like crystal part is 3-200 μm. The needle-shaped crystal part has three axes or two.
Although some of the shafts are also mixed, these are the result of contact with other whiskers during or after growth, a part of which is broken, or the growth stops. In addition, some tetrapods are attached to other parts of the complete tetrapod due to the contact during the growth. According to the manufacturing method of the present invention, a tetrapod-like one is mainly used, although other shapes, that is, plate-like crystals may adhere in a needle state.
本発明者は針状部の寸法が前述の如く細く短く、かつ
二次成長部を付着させた従来の結晶体から飛躍的に巨大
でかつて実現されたことのない巨大テトラポッド状ウィ
スカー集合体を発現させるべく種々実験研究の結果、そ
の製造方法に極めて大きな要因あることを認識した。The present inventor has developed a giant tetrapod-like whisker aggregate that has a needle size that is extremely thin and short as described above, and that has never been realized before, and is dramatically huge from the conventional crystal having the secondary growth portion attached thereto. As a result of various experimental studies to express this, it was recognized that there was an extremely large factor in the production method.
更に詳細には従来法の如く、インゴットからの亜鉛金
属溶湯や、還元亜鉛、亜鉛化合物からの純金属亜鉛等を
使用しての焼成雰囲気条件の選定だけでは上記巨大テト
ラポッド状ウィスカーを発現させることが不可能であ
り、これを達成させるには、従来と異なり、亜鉛金属粉
末、特に表面に酸化皮膜を有する亜鉛粉末を用いるのが
必須であり、かつ、この粉末を用いて上記の容器を用い
た加熱酸化方法を採ることにより、容器の上層部にウィ
スカーを下層に団魂状酸化亜鉛粉末を堆積させる反応方
式により上層部に新規な巨大テトラポッド状酸化亜鉛ウ
ィスカーの集合体が発現することを確認した。More specifically, as in the conventional method, the selection of firing atmosphere conditions using molten zinc metal from an ingot, reduced zinc, pure metal zinc from a zinc compound, or the like allows the above giant tetrapod-like whisker to be developed. In order to achieve this, it is essential to use zinc metal powder, especially zinc powder having an oxide film on the surface, and to use the above-mentioned container using this powder. By adopting the heat oxidation method, a new giant tetrapod-like zinc oxide whisker aggregate appears in the upper layer by a reaction method in which whiskers are deposited on the upper layer of the container and gang-like zinc oxide powder is deposited on the lower layer. confirmed.
更に詳細には、本発明の製造方法の中で、表面に酸化
皮膜を有する亜鉛金属粉末の酸化皮膜部が内部亜鉛金属
部からの亜鉛蒸気、煙に対し密封性を示す。即ち密封度
の高い酸化皮膜を有する粉末は、低い密封度のものより
低温域では蒸気、煙の発生が抑制され、高温域で一気に
高濃度の亜鉛煙、蒸気の発生、追随した酸化反応が起こ
り、本発明の酸化亜鉛ウィスカーが発現する。又この酸
化皮膜の別の効果の一つは亜鉛金属部が互いに融解、溶
湯化することなく、高濃度の亜鉛煙、蒸気を発生させる
ことである。More specifically, in the production method of the present invention, the oxide film portion of the zinc metal powder having an oxide film on the surface shows sealing properties against zinc vapor and smoke from the internal zinc metal portion. In other words, the powder having an oxide film with a high sealing degree suppresses the generation of steam and smoke in a lower temperature range than that of a powder with a low sealing degree, and the generation of high-concentration zinc smoke and steam at a stretch in a high temperature range, and the following oxidation reaction occurs. Thus, the zinc oxide whiskers of the present invention are expressed. Another effect of the oxide film is to generate high-concentration zinc smoke and vapor without melting and melting the zinc metal parts with each other.
即ちこの酸化皮膜は内部からの亜鉛煙、蒸気の発生を
制御する役割を有する結果である。又第3に皮膜の酸化
亜鉛部がウィスカー成長の基板的役割を担っていること
も同時に確認された。尚上述の密封度とは粉末内部の亜
鉛金属からの蒸気、煙を表面で密封する度合をいう。こ
れは酸化皮膜の厚み、組織、金属部と酸化皮膜部の体積
比等により変化する。That is, this oxide film has a role of controlling the generation of zinc smoke and vapor from the inside. Thirdly, it was simultaneously confirmed that the zinc oxide portion of the film played a role of a substrate for whisker growth. The above-mentioned degree of sealing refers to the degree of sealing vapor and smoke from zinc metal inside the powder on the surface. This varies depending on the thickness and structure of the oxide film, the volume ratio between the metal portion and the oxide film portion, and the like.
特に酸化皮膜の厚み、組織は金属粉末の製造時に達成
されるものが多い。即ち溶融亜鉛粉末を経て得られるも
のは特に制御しない限り、厚くてやや多孔質な酸化皮膜
が得られる。逆に固体のまま粉砕した系では皮膜厚は小
でかなりち密なものが得られる。又これら膜厚の均等性
は前者のものの方が良好であるが、後者の場合は形状が
やや複雑で凹凸部を有する粉末形となるため、膜厚が不
均一となる場合も多い。又前者の場合、膜厚が厚く成長
し過ぎた場合は表面部がぜい弱となり、クラックを生じ
欠陥を生じさせることもある。又このような酸化皮膜を
有する粒子系では、以上の様な条件以外でも、転移、そ
の他の要因で皮膜に欠陥を生じることも多い。In particular, the thickness and texture of the oxide film are often achieved during the production of metal powder. That is, a thick and somewhat porous oxide film can be obtained from the material obtained through the molten zinc powder unless otherwise controlled. Conversely, in a system pulverized as a solid, the film thickness is small and a very dense one can be obtained. In addition, the uniformity of the film thickness is better in the former case, but in the latter case, since the shape is slightly complicated and the powder form has irregularities, the film thickness is often non-uniform. In the former case, if the film thickness is too large, the surface becomes weak and cracks may occur to cause defects. In addition, in the particle system having such an oxide film, a defect often occurs in the film due to dislocation or other factors other than the above conditions.
次にこれら皮膜の欠陥、割れ等密封性の劣化を改修し
たり、膜厚を増大させたりするためには、擂潰、熟成処
理を行う。この処理は選択的に上述欠陥部が膜欠損部に
酸化物を堆積させることを確認した。Next, in order to repair the deterioration of the sealing properties such as defects and cracks of the film and to increase the film thickness, crushing and aging treatments are performed. This processing selectively confirmed that the above-mentioned defect portion deposited oxide on the film defect portion.
更にこれらの亜鉛粉末について詳記する。これらの粒
子径は0.1〜500μmのものが使用可能であり、なかでも
10〜300μmのものが最良の結果となる。これらの金属
亜鉛粉末は亜鉛線、亜鉛棒や亜鉛粉末をガス溶線法、ガ
ス溶棒法、ガス粉末法、電気(アーク)溶線法、プラズ
マジェット法等で空気中に溶射することより得た粉末、
溶湯粉化によるもの、即ち粒状化法、アトマイズ法によ
る粉末がある。又機械的粉砕による方法即ち、地金イン
ゴット等を切削又はジョー・クラッシャー、ジャイレー
トリ・クラッシャーで粗粉砕されたものを更に再粉砕し
たものがあり、その中粉砕にはいろいろの形式がある
が、スタンプミル法、渦流ミル法等がある。更により微
細粉にするためにはハンマーミル、カッチングミル、ミ
クロナイザー等を使用して得た粉末がある。又電解によ
るもの、金属の蒸発、凝固剤を利用した物理的操作、化
学的反応を利用した化学操作による亜鉛粉末を用いるこ
ともできる。通常は、上記の各方法での粉末では粉末表
面に酸化皮膜が生成しない様に留意して製造されている
が、本発明に使用する場合には逆に酸化皮膜が表面に形
成されれば有効であるため、水分共存下や高酸素濃度
(大気中等)高湿度中等の酸化促進雰囲気中で製造する
ことも可能である。又高温、高機械的圧力下で製造する
場合にも良好な粉末を得ることができる。又、上記の亜
鉛粉末製造法を採っても密封性の点で酸化皮膜形成が不
充分な場合や、酸化皮膜が有効な程に形成されない粉末
製造法が採られた場合には以下に示す好ましい方法が採
られる。Further, these zinc powders will be described in detail. Those having a particle diameter of 0.1 to 500 μm can be used, and among them,
10-300 μm gives the best results. These metallic zinc powders are powders obtained by spraying zinc wire, zinc rods or zinc powders into the air by a gas melting method, a gas melting method, a gas powder method, an electric (arc) melting method, a plasma jet method or the like. ,
There are powders obtained by powdering molten metal, that is, powders obtained by a granulation method and an atomizing method. Also, there is a method by mechanical pulverization, that is, a method in which a metal ingot is cut or coarsely pulverized by a jaw crusher or a gyratory crusher and further crushed again. There are a mill method and a vortex mill method. Further finer powders include powders obtained using a hammer mill, a cutting mill, a micronizer or the like. It is also possible to use zinc powder obtained by electrolysis, evaporation of metal, physical operation using a coagulant, or chemical operation using a chemical reaction. Normally, powders manufactured by the above-described methods are manufactured so that an oxide film is not formed on the surface of the powder, but when used in the present invention, it is effective if an oxide film is formed on the surface. Therefore, it can be produced in an oxidation-promoting atmosphere such as in the presence of moisture or in a high oxygen concentration (such as in the air) and high humidity. Also, a good powder can be obtained when producing under high temperature and high mechanical pressure. In addition, even if the above-described zinc powder production method is adopted, when an oxide film is insufficiently formed in terms of sealing properties, or when a powder production method in which an oxide film is not formed to an effective degree is employed, the following preferable method is used. A method is adopted.
まず水共存下での機械的処理として乳鉢式擂潰機、ロ
ール等で処理を行い粒子に圧力を加える。更にこれを水
中に24時間以上、なかでも76時間ならばいかなる粒子径
のものでも完全な結果を与える。又放置熟成温度は20℃
以上に保つことが好ましい。酸化皮膜の形成は上記メカ
ノケミカル反応によらなくても熟成等によるケミカル反
応だけでも形成できるが、通常後者の場合は時間がかか
りすぎるし、上述、密封度向上には前者の方の効果が大
きい。First, as a mechanical treatment in the coexistence of water, the particles are treated with a mortar-type crusher, roll, or the like, and pressure is applied to the particles. In addition, it can give perfect results in any particle size for more than 24 hours in water, especially 76 hours. Aging temperature is 20 ℃
It is preferable to keep the above. The formation of an oxide film can be formed only by a chemical reaction such as aging without relying on the mechanochemical reaction described above, but the latter usually takes too much time, and the former has a greater effect in improving the sealing degree as described above. .
このように酸化皮膜の形成、増大、成長の要因は多岐
にわたるが総括すると(1)機械的圧力の付加、(2)
水中ないし高湿度下での酸化反応、(3)、(1)
(2)の相乗効果(メカノケミカル反応)、(4)酸素
濃度、(5)温度効果等が関係する。生成するウィスカ
ーの寸法、特に針状部の長さ径から評定すると、上記
(3)による時間が大きく影響を与える。即ち短時間で
効果は大である。As described above, the factors of the formation, increase, and growth of the oxide film are various, but when summed up, (1) application of mechanical pressure, (2)
Oxidation reaction in water or under high humidity, (3), (1)
The synergistic effect of (2) (mechanochemical reaction), (4) oxygen concentration, (5) temperature effect, etc. are related. When evaluated from the size of the whisker to be generated, especially the length of the needle-shaped portion, the time according to the above (3) greatly affects. That is, the effect is large in a short time.
水との共存下での擂潰、熟成時間が大ならば上記ウィ
スカー寸法も原料粉の酸化皮膜の密封度向上により、増
大する傾向にある。If the crushing and aging time in the coexistence with water is long, the whisker size tends to increase due to the improvement in the sealing degree of the oxide film of the raw material powder.
粉体上の酸化皮膜は密封度向上により、内部の金属亜
鉛部からの亜鉛の放出を低温域で抑制するし又内部への
酸素の移行も同様に抑制する。このため単結晶成長時に
十分な亜鉛蒸気、煙濃度が与えられる。結晶寸法は従来
の気相法のものとかけ離れて画期的に大きくなる。The oxide film on the powder suppresses the release of zinc from the metal zinc portion in the low temperature range and also suppresses the transfer of oxygen to the inside by improving the sealing degree. Therefore, sufficient zinc vapor and smoke density are provided during single crystal growth. The crystal size is significantly different from that of the conventional gas-phase method and is remarkably large.
次に放置熟成後乾燥する。この乾燥は粉末表面の水切
りが達成できればよく、次の焼成工程の高温中へ移行し
た当初の弊害が防がれるように、即ち、ルツボ割れ、粉
末の飛び散りがなくなる程度に乾燥すれば良好である。
このために風乾ないし亜鉛粉末が溶融しない高温迄の温
度範囲で行うことができる。Next, it is dried after aging. This drying may be achieved as long as the powder surface can be drained, and it is preferable to dry the powder so as to prevent the adverse effects at the beginning of the transition to a high temperature in the next firing step, that is, to such an extent that crucible cracking and powder scattering do not occur. .
For this reason, it can be performed in a temperature range from air drying to a high temperature at which the zinc powder does not melt.
次に乾燥した亜鉛粉末は、本発明に用いる耐熱性容器
の底部に散布して焼成、酸化する。上記容器とは金属、
カーボン、磁器(アルミナ)等の素材より得られるもの
で、底部に対応した開口面を有する。Next, the dried zinc powder is sprayed on the bottom of the heat-resistant container used in the present invention, baked and oxidized. The container is metal,
It is obtained from a material such as carbon or porcelain (alumina) and has an opening surface corresponding to the bottom.
又、上記素材が各々無孔質のち密面から達成されたも
のや多孔質からなるものも含む。具体的には、これら容
器がルツボである場合も含む。次に原料を底部に配置し
た容器を予め加熱した酸素を含む雰囲気を保持した炉内
に導き焼成、酸化を行う。又炉内温度は700〜1300℃、
中でも900〜1100℃で加熱するのが、いかなる粒子径で
も良好な結果を与える。In addition, the above-mentioned materials include those obtained from a nonporous and dense surface and those made of a porous material. Specifically, the case where these containers are crucibles is also included. Next, the container in which the raw material is disposed at the bottom is guided into a furnace holding a preheated atmosphere containing oxygen, followed by firing and oxidation. The furnace temperature is 700 ~ 1300 ℃,
Among them, heating at 900 to 1100 ° C. gives good results at any particle size.
又、上記温度域の炉内に前記ルツボを保持しておき、
調整した粉末を投入して散布して焼成しても好ましい結
果を与える。焼成時間は700〜1300℃において120〜10分
間、900〜1100℃では90〜10分間が適当である。前記加
熱焼成は通常空気中で行えば良いが、窒素と酸素の混合
比を調整したガスや酸素ガスを用いても好ましい結果と
なる。Also, holding the crucible in the furnace in the above temperature range,
Preferable results are also obtained by feeding the adjusted powder, spraying and firing. The firing time is suitably from 120 to 10 minutes at 700 to 1300 ° C, and from 90 to 10 minutes at 900 to 1100 ° C. The heating and sintering may be usually performed in air, but a preferable result is obtained by using a gas or oxygen gas in which the mixture ratio of nitrogen and oxygen is adjusted.
上記加熱酸化の特に初期過程では加熱された亜鉛粉末
は容器の応部から開口部へと飛び上り、開口部付近から
底部へと落下してくる。これを繰り返しながら酸化反応
とウィスカー成長が進み、次第に容器上層部には本発明
のウィスカー集合体が堆積し下層には団魂状酸化亜鉛粉
末が堆積する。Particularly in the initial stage of the thermal oxidation, the heated zinc powder jumps up from the corresponding portion of the container to the opening, and falls from the vicinity of the opening to the bottom. By repeating this, the oxidation reaction and whisker growth proceed, and the whisker aggregate of the present invention is gradually deposited on the upper layer of the container, and the gang-like zinc oxide powder is deposited on the lower layer.
以上の様に本発明の製造方法が達成されるには、前述
の様に密封性酸化皮膜を有する亜鉛粉末が必須となる。
これは各種の粉末製造方法やその条件制御により密封性
の酸化皮膜が発現できるし、更に水共存下での擂潰、熟
成処理により、完全化される。As described above, in order to achieve the production method of the present invention, a zinc powder having a sealing oxide film as described above is essential.
This can form a sealing oxide film by various powder production methods and the control of the conditions, and can be completed by crushing and aging treatment in the presence of water.
この事実は、X線回折、電子顕微鏡観察より確認し
た。又、この様に形成された酸化皮膜又はこれらの処理
では焼成工程に特別な効果を与えている。This fact was confirmed by X-ray diffraction and electron microscope observation. In addition, the oxide film formed in this way or these treatments have a special effect on the firing step.
すなわち、亜鉛粉末が酸化を受けない良好な方法で製
造された直後のもので、酸化皮膜の形成がないもの、或
はX線回折法では全く検出できない極めて薄くぜい弱な
膜しか有さないものでは、前記条件下の焼成時に均等に
粒子の飛上昇、降下が起こらなく、不均一焼成となり、
温度、酸素濃度を調整しても種々の色調の団魂状酸化亜
鉛と未燃焼の金属亜鉛が共存した系が生成し、ウィスカ
ーは生成しない。That is, immediately after the zinc powder is manufactured by a good method that does not undergo oxidation, there is no formation of an oxide film, or there is only an extremely thin and weak film that cannot be detected by X-ray diffraction. In the firing under the above conditions, the particles do not rise and fall evenly, resulting in uneven firing,
Even when the temperature and the oxygen concentration are adjusted, a system in which zinc oxide having various colors and unburned metallic zinc coexist is generated, and whiskers are not generated.
一方、成長した密封性酸化皮膜を有する亜鉛粉末で
は、高温焼成が均一かつ完全に進行して極めて高収率に
巨大テトラポッド状ウィスカーに成長するし、皮膜部の
酸化物は層状に団魂状酸化亜鉛となり生成する。On the other hand, in the case of zinc powder with a grown sealing oxide film, high-temperature sintering proceeds uniformly and completely to grow into giant tetrapod-like whiskers with extremely high yield, and the oxide in the film part is in a layered shape Generates as zinc oxide.
この様に亜鉛粉末が酸化皮膜により完全に覆われてい
る場合には、テトラポット状ウィスカーは完全に成長
し、形状的にも二次成長部や板状晶等が少なくなる。こ
のため製造時に酸化皮膜が形成され、更に擂潰、熟成に
よる皮膜形成を促した系では、形状、大きさ共に良好な
ウィスカー集合体を得ることができる。しかるに皮膜の
密封度は前述の如く膜厚のみで一義的に決定できなく、
特に大きさ、寸法に関しては、膜の組織金属部の体積比
(粒径に依存)等により変化する。このため局部的に酸
化皮膜が形成されている場合でも本発明のテトラポット
状ウィスカーを得ることは可能であるが、形状、収率が
かなり低位となる。When the zinc powder is completely covered with the oxide film as described above, the tetrapod-like whiskers grow completely, and the number of secondary growth portions, plate crystals, and the like is reduced in shape. For this reason, an oxide film is formed at the time of manufacture, and in a system in which the formation of a film is further promoted by crushing and aging, a whisker aggregate having a good shape and size can be obtained. However, the sealing degree of the film cannot be uniquely determined only by the film thickness as described above,
In particular, the size and size vary depending on the volume ratio (depending on the particle size) of the tissue metal part of the film. For this reason, it is possible to obtain the tetrapod-like whisker of the present invention even when an oxide film is locally formed, but the shape and the yield are considerably low.
又、焼成製造時、加工調整された粉末のみかけ体積に
比し、ウィスカー生成系は急激に体積を増大するが、通
常の気相成長法で通常みられるソース部外へのウィスカ
ーの付着発現、成長のタイプではなく、基本的に大部分
のものは原料設置部分に連続的に生成、成長する体積増
加型のものである。In addition, during sintering, the whisker generation system rapidly increases in volume compared to the apparent volume of the processed powder, but the appearance of whiskers outside the source part, which is usually observed in normal vapor phase epitaxy, Basically, most are not of the growth type, but are of the volume increasing type which is continuously generated and grown in the material setting portion.
実施例 以下に本発明の実施例を示す。Examples Examples of the present invention will be described below.
実施例1 純度99.99%の亜鉛線をアーク放電方式による溶射法
で、酸素濃度27%の酸素、窒素混合ガス雰囲気中に溶射
した。雰囲気の温度は40℃に設定して行った。Example 1 A zinc wire having a purity of 99.99% was sprayed in an oxygen-nitrogen mixed gas atmosphere having an oxygen concentration of 27% by a spraying method using an arc discharge method. The temperature of the atmosphere was set at 40 ° C.
この亜鉛粉末を回収し粒子径を150〜300μmに分級し
て、再度150℃で24時間乾燥して焼成に供した。この粉
末120gを容器としては多孔質アルミナ磁器製のルツボの
底面に散布した。このアルミナルツボは長方体で横20c
m、縦35cm、高さ15cmであり、広面積部の一面が開口部
となっている。又上記粉末はこの開口面に対応する底面
に3mm厚で上記粉末を均一散布した。この容器をそのま
ま予め960℃に保たれた炉内に導き空気雰囲気で35分間
の加熱処理を行った。この結果、上記容器内の下層部に
は、やや黄色の団魂状酸化亜鉛が層状に生成され、その
上層部にはみかけ嵩比重0.11の巨大テトラポッド状酸化
亜鉛ウィスカー集合体が生成した。わずかにウィスカー
層が容器外にあふれたが、反応の主体は容器内で行わ
れ、反応初期の高温亜鉛粉末粒子が開口部分の距離まで
上昇し降下する現像を繰り返しながら酸化反応ウィスカ
ー生成反応が続行した。この時上記の如く容器外に多少
あふれることがあるが、反応の主体は容器内で行われ、
生成物のほとんどは容器内に堆積した。The zinc powder was recovered, classified into a particle size of 150 to 300 μm, dried again at 150 ° C. for 24 hours, and provided for firing. 120 g of this powder was sprayed on the bottom of a crucible made of porous alumina porcelain as a container. This alumina crucible is rectangular and 20c wide
m, length 35 cm, height 15 cm, one side of the wide area is an opening. The powder was evenly sprayed on the bottom surface corresponding to the opening surface in a thickness of 3 mm. This container was directly introduced into a furnace maintained at 960 ° C. in advance, and subjected to a heat treatment in an air atmosphere for 35 minutes. As a result, a somewhat yellow band-like zinc oxide was formed in a layer in the lower part of the container, and a giant tetrapod-like zinc oxide whisker aggregate having an apparent bulk density of 0.11 was formed in the upper part. The whisker layer slightly overflowed outside the container, but the main reaction took place in the container, and the oxidation whisker generation reaction continued while repeating the development in which the high-temperature zinc powder particles in the initial stage of the reaction rise and fall down to the distance of the opening. did. At this time, there may be some overflow outside the container as described above, but the main body of the reaction is performed in the container,
Most of the product deposited in the vessel.
生成酸化亜鉛中の上記ウィスカー集合体の割合は88%
であり、残り12%で団魂状酸化亜鉛であった。得られた
酸化亜鉛ウィスカーの電子顕微鏡写真を第1図に示す。88% of the above whisker aggregates in the generated zinc oxide
And the remaining 12% was zinc oxide. An electron micrograph of the obtained zinc oxide whiskers is shown in FIG.
核部と、この核部から異なる4軸方向に伸びた針状結
晶部からなるテトラポッド状の結晶体が明確に認められ
る。又板状晶のものも認められた。いずれにしても上記
の方法によると巨人テトラポッド状のものが85%以上を
占める。第2図は上記ウィスカーのX線回折図を示す。
すべて酸化亜鉛のピークを示し、電子線回折の結果も、
転移、格子欠陥の少ない単結晶性を示した。又不純物含
有量も少なく、原子吸光分析の結果、酸化亜鉛が99.97
%であった。A tetrapod-like crystal composed of a nucleus and needle-like crystal parts extending from the nucleus in four different directions is clearly recognized. Plate-like crystals were also observed. In any case, according to the above method, giant tetrapods account for 85% or more. FIG. 2 shows an X-ray diffraction diagram of the whisker.
All show zinc oxide peaks, and the results of electron diffraction
It showed single crystallinity with few transitions and lattice defects. In addition, the content of impurities is small, and as a result of atomic absorption analysis, zinc oxide is 99.97
%Met.
実施例2 実施例1と同じ純亜鉛線を同じ溶射法で溶射し、直
後、その粉末を回収し、粉末1Kgに対し550gのイオン交
換水を投入し、乳鉢型擂潰機で25分間攪拌処理を行い、
次に20℃の水中に75時間放置熟成した。放置時の水量粉
体層から約1cmの水位を保って大気中で保管した。この
水中放置後、130℃で3時間の乾燥を行うことにより、
粉末の水分を除去する。次にこの粉末を多孔質アルミナ
容器に入れ、底面に散布した。容器は横40cm、縦50cm、
高さ30cmであり、広面積の一面が開口部となっている。
粉末散布方法は上記亜鉛粉末200gを3mm以下の厚みで均
一に散布した。この容器をそのまま予め970℃に保たれ
た炉内に導き、30分間、焼成、酸化させた。堆積物の様
子や反応中の亜鉛粒子の振るまいは実施例1と同様であ
った。上層部のウィスカーの嵩比重は0.09巨大のテトラ
ポッド状酸化亜鉛ウィスカー集合体であった。割合は84
%であった。得られた酸化亜鉛ウィスカーの電子顕微鏡
写真を第3図に示す。4軸テトラポッド状のものが89%
以上を占める。X線回折、電子線回折の結果は実施例1
と同様であった。原子吸光分析では酸化亜鉛が99.99wt
%以上であった。Example 2 The same pure zinc wire as in Example 1 was sprayed by the same thermal spraying method. Immediately after that, the powder was recovered, 550 g of ion-exchanged water was added to 1 kg of the powder, and the mixture was stirred with a mortar-type mortar for 25 minutes. Do
Next, it was left to mature in water at 20 ° C. for 75 hours. The amount of water at the time of standing The water level was kept about 1 cm from the powder layer and stored in air. After leaving in water, drying at 130 ° C for 3 hours
Remove moisture from powder. Next, this powder was placed in a porous alumina container and sprayed on the bottom surface. The container is 40 cm wide, 50 cm long,
The height is 30 cm, and one side of the wide area is an opening.
In the powder spraying method, 200 g of the above zinc powder was uniformly sprayed with a thickness of 3 mm or less. This vessel was directly introduced into a furnace maintained at 970 ° C. in advance, and calcined and oxidized for 30 minutes. The state of the deposit and the behavior of the zinc particles during the reaction were the same as in Example 1. The bulk density of the whiskers in the upper layer was 0.09 giant tetrapod-like zinc oxide whisker aggregates. Ratio is 84
%Met. An electron micrograph of the obtained zinc oxide whiskers is shown in FIG. 89% of 4-axis tetrapods
Account for the above. The results of X-ray diffraction and electron diffraction are shown in Example 1.
Was similar to 99.99wt zinc oxide by atomic absorption spectrometry
% Or more.
実施例3 機械的粉砕による粉末を使用した。純度99.99%以上
の地金を切削し、ショークラッシャーで5回粗粉砕した
後、スタンプミルで10回微粉砕した。全て空気中で行っ
た。粒子径50〜300μmのものを分級して得た。焼成炉
温度は970℃で、酸素25%の窒素混合ガス雰囲気で行っ
た。時間は35分間とした。容器は炭化硅素製で、横20c
m、縦40cm、高さ20cmの直方体で広面積の一面が開口部
となっている。他は全て実施例1と同様に行った。みか
け嵩比重0.1でのウィスカーが84wt%得られ、16wt%が
団魂状酸化亜鉛であった。このウィスカーの電子顕微鏡
写真を第4図に示す。4軸テトラポッド状のものが81%
であった。X線、電子線回折の結果は実施例1と同様で
あった。ウィスカーの原子吸光分析で酸化亜鉛が99.97
%であった。Example 3 A powder obtained by mechanical pulverization was used. Metal having a purity of 99.99% or more was cut, coarsely pulverized 5 times with a show crusher, and finely pulverized 10 times with a stamp mill. All performed in air. Particles having a particle diameter of 50 to 300 μm were obtained by classification. The firing temperature was 970 ° C. in a nitrogen mixed gas atmosphere of 25% oxygen. The time was 35 minutes. Container is made of silicon carbide, 20c wide
It is a rectangular parallelepiped of m, 40cm in height and 20cm in height. All other steps were the same as in Example 1. A whisker with an apparent bulk specific gravity of 0.1 was obtained in an amount of 84% by weight, and 16% by weight of the whisker was a reticulated zinc oxide. An electron micrograph of this whisker is shown in FIG. 81% of 4-axis tetrapods
Met. X-ray and electron diffraction results were the same as in Example 1. Atomic absorption spectroscopy of whisker shows 99.97 zinc oxide
%Met.
実施例4 実施例3と同様に機械的粉砕による粉末を得た。更に
この粉末1Kgに対し500gのイオン交換水を加え、乳鉢式
擂潰機で10分間攪拌処理を行い、次に25℃の水中に90時
間放置、熟成する。水中放置後、150℃で12時間乾燥し
粉末の水分を除去した。この様に調整した粉末を実施例
3と同様に焼成処理した。生成したウィスカーの嵩比重
は0.09で75wt%が得られ、25%が団魂状酸化亜鉛粉末で
あった。このウィスカーの電子顕微鏡写真を第5図に示
す。4軸テトラポッド状のものが92%を示した。X線、
電子線回析の結果は実施例1と同様であった。ウィスカ
ーの原子吸光分析で酸化亜鉛が99.99wt%であった。容
器は実施例3と同様にして同様な反応形態で行われた。Example 4 A powder was obtained by mechanical pulverization in the same manner as in Example 3. Further, 500 g of ion-exchanged water is added to 1 kg of the powder, and the mixture is stirred for 10 minutes in a mortar-type grinder, and then left in water at 25 ° C. for 90 hours for aging. After standing in water, the powder was dried at 150 ° C. for 12 hours to remove water from the powder. The powder thus adjusted was fired in the same manner as in Example 3. The resulting whiskers had a bulk specific gravity of 0.09, yielding 75% by weight, and 25% were dandelion-shaped zinc oxide powder. An electron micrograph of this whisker is shown in FIG. Those with four-axis tetrapods showed 92%. X-ray,
The result of electron beam diffraction was the same as in Example 1. Atomic absorption analysis of whiskers indicated that zinc oxide was 99.99% by weight. The vessel was used in the same reaction mode as in Example 3.
実施例5 揮発、凝縮法による球状亜鉛粉末を用いた。磁器製容
器中に純度99.97wt%の亜鉛地金を入れ970℃に保ち亜鉛
を蒸発させ気化分を室温、空気中で凝縮させた。平均粒
径7.5μmのものを分級して得た。この亜鉛粉末を実施
例1と同様にして焼成した。焼成用容器は実施例1と同
寸法の炭化硅素製のものであり、実施例1と同様にして
焼成した。但し焼成温度は990℃で25分間行った。雰囲
気は空気であった。反応中の亜鉛粒子の挙動は実施例1
と同様で生成物の堆積も同様であった。Example 5 A spherical zinc powder obtained by a volatilization and condensation method was used. 99.97% by weight of zinc ingot was put in a porcelain container and kept at 970 ° C. to evaporate zinc and condense vaporized components in air at room temperature. The particles having an average particle size of 7.5 μm were obtained by classification. This zinc powder was fired in the same manner as in Example 1. The firing container was made of silicon carbide having the same dimensions as in Example 1, and was fired in the same manner as in Example 1. However, the firing temperature was 990 ° C. for 25 minutes. The atmosphere was air. The behavior of the zinc particles during the reaction is shown in Example 1.
The product deposition was similar.
生成ウィスカーの嵩比重0.09で92wt%が得られた。他
は団魂状酸化亜鉛であった。このウィスカーの電子顕微
鏡写真を第6図に示す。4軸テトラポッド状のものは90
%以上であった。又実施例4までのものより針状部の寸
法が小であった。X線、電子線回折、原子吸光分析の結
果も実施例1と同様であった。92% by weight was obtained at a bulk specific gravity of the produced whiskers of 0.09. The others were gang-like zinc oxide. An electron micrograph of this whisker is shown in FIG. 90 for 4-axis tetrapod
% Or more. In addition, the size of the needle-shaped part was smaller than that of Example 4. The results of X-ray, electron diffraction and atomic absorption analysis were the same as in Example 1.
実施例6 実施例5で用いた亜鉛粉末を用いた。この粉末1Kgを5
50mlの水中に投じ、擂潰機で5分間混合した。次に30℃
の水中に91時間放置熟成した。その後110℃で24時間乾
燥して水分を除去した。この様に調整した粉末を実施例
5と同様に同条件で酸化させた。生成したウィスカーの
嵩比重0.09で84wt%で得られ、残りは団魂状酸化亜鉛で
あった。ウィスカーの電子顕微鏡写真を第7図に示す。
4軸テトラポッド状のものは95%以上であった。実施例
5と同様に針状部寸法がその他のものよりやや小であっ
た。X線、電子線回折、原子吸光分析の結果も実施例1
と同様であった。Example 6 The zinc powder used in Example 5 was used. 1 kg of this powder to 5
It was thrown into 50 ml of water and mixed for 5 minutes with a crusher. Then 30 ℃
And aged in water for 91 hours. Thereafter, drying was performed at 110 ° C. for 24 hours to remove water. The powder thus adjusted was oxidized under the same conditions as in Example 5. The resulting whiskers had a bulk specific gravity of 0.09 and were obtained at 84 wt%, with the balance being zinc oxide. An electron micrograph of the whiskers is shown in FIG.
The ratio of the tetraaxial tetrapods was 95% or more. As in the case of Example 5, the size of the needle-like portion was slightly smaller than those of the others. The results of X-ray, electron diffraction and atomic absorption analysis are also shown in Example 1.
Was similar to
上記実施例を次表にまとめる。 The above examples are summarized in the following table.
発明の効果 本発明の製造方法によると巨大テトラポッド状の酸化
亜鉛ウィスカーが得られる。又製造方法として原料とし
て表面に、酸化皮膜を有する亜鉛粉末の粒度選択、酸化
皮膜の密封性の調整、水中での機械的擂潰処理、水中で
の熟成による皮膜密封度の向上処理、皮膜の厚化処理に
続き乾燥後、一面に開口面を持った容器底への原料粉末
の散布後に焼成工程で容器内にウィスカーが堆積する方
法で、酸素を含む雰囲気下で行った場合、工程条件の設
定により、テトラポッド状酸化亜鉛ウィスカーの各種の
大きさのものが得られる。 Effects of the Invention According to the production method of the present invention, zinc oxide whiskers in a giant tetrapod shape can be obtained. In addition, as a production method, as a raw material, select the particle size of zinc powder having an oxide film on the surface, adjust the sealing property of the oxide film, mechanically crush in water, improve the sealing degree of the film by aging in water, After drying after the thickening process, whiskers are deposited in the container in the baking step after spraying the raw material powder on the bottom of the container with an open surface on one side, and when performed in an atmosphere containing oxygen, the process conditions By setting, various sizes of tetrapod-like zinc oxide whiskers can be obtained.
本発明で得られるウィスカーは異方性のない立体構造
を有しているため、各種材料の強化材として用いる場合
や電子材料として用いる場合でも機械的、電気的特性に
異方性を生じさせない。又従来の酸化亜鉛の微細針状結
晶と比べて寸法的にはるかに大きく、金属や樹脂、セラ
ミックと複合させて、それらの機械的強度を強化できる
等の効果の他、他の同種目的の炭化硅素や窒化硅素等に
比べて安価に製造できる利点を有しており、工業的にも
経済的にも極めて大きな効果を奏するものである。Since the whisker obtained in the present invention has a three-dimensional structure without anisotropy, it does not cause anisotropy in mechanical and electrical characteristics even when used as a reinforcing material for various materials or when used as an electronic material. It is much larger in size than conventional fine needle crystals of zinc oxide, and can be combined with metals, resins, and ceramics to enhance their mechanical strength. It has the advantage of being inexpensive to produce compared to silicon, silicon nitride, etc., and has an extremely large industrial and economical effect.
第1図および第3〜7図は本発明による酸化亜鉛ウィス
カーの結晶構造を示す電子顕微鏡写真、第2図はX線回
折図である。1 and 3 to 7 are electron micrographs showing the crystal structure of the zinc oxide whiskers according to the present invention, and FIG. 2 is an X-ray diffraction diagram.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 八木 順 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (72)発明者 吉田 英行 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (72)発明者 佐藤 隆重 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 ──────────────────────────────────────────────────の Continued on the front page (72) Inventor Jun Yagi 1006 Kazuma Kadoma, Osaka Prefecture Inside Matsushita Electric Industrial Co., Ltd. In-house (72) Inventor Takashige Sato 1006 Kazuma Kadoma, Kazuma, Osaka Matsushita Electric Industrial Co., Ltd.
Claims (1)
する底面上に、表面に酸化皮膜を有する亜鉛粉末を配置
して、酸素を含む雰囲気下で加熱、酸化させて、ウィス
カーを同一容器内に生成、堆積させることを特徴とする
酸化亜鉛ウィスカーの製造法。1. A container having an opening on one surface, a zinc powder having an oxide film on the surface is disposed on a bottom surface corresponding to the opening, and heated and oxidized in an atmosphere containing oxygen to form a whisker. Whiskers are produced and deposited in the same container.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63328271A JP2584035B2 (en) | 1988-12-26 | 1988-12-26 | Method for producing zinc oxide whiskers |
| DE68924646T DE68924646T2 (en) | 1988-12-16 | 1989-12-13 | METHOD FOR PRODUCING ZINCOXIDE WHISKERS. |
| KR1019900701787A KR930007857B1 (en) | 1988-12-16 | 1989-12-13 | Production method of zinc-oxide whisker |
| US07/566,475 US5158643A (en) | 1988-12-16 | 1989-12-13 | Method for manufacturing zinc oxide whiskers |
| PCT/JP1989/001246 WO1990007022A1 (en) | 1988-12-16 | 1989-12-13 | Production method of zinc oxide whisker |
| EP90900992A EP0407601B1 (en) | 1988-12-16 | 1989-12-13 | Production method of zinc oxide whisker |
| CA002005737A CA2005737C (en) | 1988-12-16 | 1989-12-15 | Manufacturing method of zinc oxide whiskers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63328271A JP2584035B2 (en) | 1988-12-26 | 1988-12-26 | Method for producing zinc oxide whiskers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02172897A JPH02172897A (en) | 1990-07-04 |
| JP2584035B2 true JP2584035B2 (en) | 1997-02-19 |
Family
ID=18208361
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63328271A Expired - Lifetime JP2584035B2 (en) | 1988-12-16 | 1988-12-26 | Method for producing zinc oxide whiskers |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2584035B2 (en) |
-
1988
- 1988-12-26 JP JP63328271A patent/JP2584035B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02172897A (en) | 1990-07-04 |
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