Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0212883B2 - - Google Patents
[go: Go Back, main page]

JPH0212883B2 - - Google Patents

Info

Publication number
JPH0212883B2
JPH0212883B2 JP2944682A JP2944682A JPH0212883B2 JP H0212883 B2 JPH0212883 B2 JP H0212883B2 JP 2944682 A JP2944682 A JP 2944682A JP 2944682 A JP2944682 A JP 2944682A JP H0212883 B2 JPH0212883 B2 JP H0212883B2
Authority
JP
Japan
Prior art keywords
zinc oxide
powder
particle size
average particle
heating
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
Application number
JP2944682A
Other languages
Japanese (ja)
Other versions
JPS58145620A (en
Inventor
Gohee Yoshida
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Honjo Chemical Corp
Original Assignee
Honjo Chemical Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Honjo Chemical Corp filed Critical Honjo Chemical Corp
Priority to JP2944682A priority Critical patent/JPS58145620A/en
Publication of JPS58145620A publication Critical patent/JPS58145620A/en
Publication of JPH0212883B2 publication Critical patent/JPH0212883B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Conductive Materials (AREA)

Description

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

本発明は導電性酸化亜鉛の製造方法に関する。 導電性酸化亜鉛はその導電性と共に油臭性、耐
熱性、耐光性等のすぐれた利点を有するため、静
電記録、通電記録及び放電記録によるフアクシミ
リ用記録紙やその他の情報記録用紙、産業用記録
用紙を製造する際のコーテイング剤のほか、合成
樹脂フイルムや合成繊維における導電剤として広
く用いられている。 このような導電性酸化亜鉛の製造方法は既に
種々知られている。これらのなかで代表的なもの
は、米国特許第3538022号及び第3538023号に開示
されているように、容器内でアルミニウム、ガリ
ウムインジウム、スズ等の酸化物を酸化亜鉛と共
に、還元性ガスを流通しながら、600〜900℃の温
度に加熱焼成する方法である。しかし、この方法
によれば、還元性ガスとして水素や一化炭素を用
いるから爆発の危険性がある。これを避けるため
には、還元性ガスを窒素等の不活性ガスと混合し
て、所定の非爆発性の組成を有する還元性雰囲気
下に焼成しなければならないから、工程の管理が
煩瑣となるほか、装置が複雑化し、結局、製品が
高価なものとなる。 また、従来の方法はいずれも、酸化亜鉛と活性
化剤とを水によりスラリー又はペースト状に一様
に混練した後、これを乾燥し、粉砕し、加熱焼成
する。この加熱焼成時にも原料が焼結し、粒状乃
至塊状化する傾向があるので、加熱焼成後にも再
び粉砕する必要があるが、得られる酸化亜鉛粉末
はその平均粒径が著しく大きい。 以上のように、従来の方法は煩瑣な工程管理と
多数の工程を要しながら、導電性は未だ十分とは
いえず、更に、平均粒径が大きいことから用途上
の種々の制約を受け、勿論、経済的にも非常に不
満足なものである。 このような種々の問題を解決するために、本発
明者らは既に酸化亜鉛粉末と酸化アルミニウム粉
末とを乾式混合し、固体炭素の存在下に加熱焼成
することにより、電導性の改善された酸化亜鉛を
低廉に製造する方法を提案している。(特公昭55
−19897号)。この方法によれば原料酸化物を乾式
混合して加熱焼成するので、加熱焼成の段階で原
料粉末が相互に著しく付着凝集せず、比較的微細
な導電性酸化亜鉛粉末が得られるが、平均粒径に
ついては更に小さいものが強く要求されている。
例えば、合成繊維等に使用して導電性を付与する
ためには、平均粒径が1μ以下の微粉末が可紡性
の点から好ましいとされている。しかしながら、
酸化亜鉛と酸化アルミニウムとを固体炭素の存在
下に加熱する方法においては、体積固有抵抗が数
Ω・cm乃至十Ω・cmの範囲にある導電性が改善さ
れた酸化亜鉛を得るには、原料混合粉末を900〜
1100℃の高温度で焼成することを要し、その結
果、平均粒径20mμ程度の微細な酸化アルミニウ
ムを用いても、原料粉末が相互に付着凝集する傾
向が生じて、平均粒径が1μ以下の導電性酸化亜
鉛微粉末を得ることが困難である。 一方において、導電性についても1Ω.cmより
小さい体積固有抵抗を有する更に改善された酸化
亜鉛も要求されるに至つているが、酸化アルミニ
ウムを用いる限りは、通常の処理条件下では困難
とみられる。 本発明は従来の方法における上記した問題点を
解決するためになされたものであつて、平均粒径
が1μよりも小さく、及び/又は導電性を更に改
善して体積固有抵抗が1Ω.cmよりも小さい酸化
亜鉛を製造する方法を提供することを目的とす
る。 本発明による導電性酸化亜鉛の製造方法は、酸
化亜鉛粉末と、酸化亜鉛100モルに対して0.05〜
5モルの酸化ガリウム粉末を乾式混合し、固体炭
素の存在下に700〜1100℃の温度に加熱焼成する
ことを特徴とする。 本発明において、酸化亜鉛に対する酸化ガリウ
ムの混合割合は、酸化亜鉛100モルに対して0.05
〜5モル、好ましくは0.1〜2.5モルである。酸化
ガリウムの混合割合が上記範囲より少ないとき
は、加熱焼成して得られる酸化亜鉛が高い導電性
を有さず、一方、上記範囲より多量に用いること
は経済的にも不利である。 本発明の方法は二つの側面を有する。一つの側
面は得られる酸化亜鉛の平均粒径に関し、他の側
面は得られる酸化亜鉛の体積固有抵抗に関する。
本発明を限定するものではないが、酸化亜鉛粉末
と酸化ガリウム粉末との原料混合粉末の加熱焼成
温度が高くなるにつれて、得られる導電性酸化亜
鉛の体積固有抵抗は小さくなるが、反面、その平
均粒径は大きくなる傾向が認められる。また、原
料混合物の加熱焼成温度を固定すれば、酸化亜鉛
に対する酸化ガリウムの割合が増すにつれて、得
られる導電性酸化亜鉛の体積固有抵抗がが小さく
なる傾向が認められる。従つて、本発明の方法に
よれば、好ましい場合には平均粒径が1μより小
さく、且つ、体積固有抵抗が1Ω.cmよりも小さ
い高導電性酸化亜鉛微粉末が得られる。また、必
要ならば、高温度で原料粉末を加熱焼成すること
により、平均粒径を多少犠牲にして、体積固有抵
抗が著しく小さい高導電性酸化亜鉛粉末が得られ
る。 本発明において、平均粒径が1μよりも小さい
導電性酸化亜鉛を得るには、用いる酸化亜鉛の平
均粒径が1μより小さいことを要し、好ましくは
0.1〜0.8μである。酸化ガリウム粉末は、酸化亜
鉛に対する混合量が少ないので、平均粒径は数μ
以下であればよく、通常、2μ以下の酸化ガリウ
ム粉末が好ましく用いられる。加熱焼成温度は比
較的低温であることを要し、特に700℃以上で900
℃より低い温度範囲が好ましい。このような条件
下で酸化亜鉛と酸化ガリウムを固体炭素の存在下
に加熱焼成すると、平均粒径が1μより小さい導
電性酸化亜鉛粉末が得られ、好ましい場合には平
均粒径が0.7〜0.8μであり、且つ、体積固有抵抗
も1Ω.cmより小さい高導電性酸化亜鉛微粉末が
得られる。900℃以上の高い温度で加熱焼成する
と、原料粉末が相互に付着凝集する傾向が顕著と
なるので、得られる導電性酸化亜鉛は2〜3μの
平均粒径を有するようになる。 しかし、得られる導電性酸化亜鉛粉末の平均粒
径に無関係に、その導電性の改善を目的とする場
合には、用いる酸化亜鉛粉末及び酸化ガリウム粉
末の平均粒径は特に制限されず、原料混合粉末を
850〜1100℃、酸化ガリウムの使用量の点から好
ましくは900〜1100℃の範囲の高温で加熱焼成す
るのが好ましい。このような条件下での処理によ
り、1Ω・cmより小さい体積固有抵抗を有する高
導電性酸化亜鉛粉末を得ることができる。前記し
たように、800℃以下の低い温度で加熱焼成すれ
ば、平均粒径が1μより小さい導電性酸化亜鉛微
粉末が得られるが、反面、それが有する体積固有
抵抗は数Ω・cm乃至数十Ω.cmであつて、1Ω.
cm以下に小さくすることが困難であるからであ
る。 尚、本発明の二つの側面はいずれにおいても、
1100℃を越える高い温度に加熱すると、金属亜鉛
の生成が顕著となり、目的とする導電性酸化亜鉛
の収量が低下する不利益も生じるので好ましくな
い。また、本発明においては、必要ならば、酸化
ガリウムに代えて、又は酸化ガリウムと共に、処
理条件下で酸化ガリウムを生成し得るガリウム化
合物を用いることができる。 酸化亜鉛粉末と酸化ガリウム粉末を乾式混合す
るには、例えば、V型混合機のような回転容器型
混合機や、リボン型、スクリユー型、回転刃型そ
の他の固定容器型混合機を適宜に用いることがで
きる。酸化亜鉛粉末と酸化ガリウム粉末を均一に
乾式混合できれば、混合方法は特に限定されな
い。また、加熱焼成時間は通常、15分から5時間
程度である。 固体炭素としては、例えば、粉状、粒状又は塊
状の木炭が好適である。このような固体炭素は酸
化亜鉛と酸化ガリウムの原料混合粉末と隔離し
て、又は混合して、上記混合粉末と共に容器内で
加熱する。固体炭素を原料混合粉末と混合して加
熱する場合には、この炭素は、原料混合粉末の加
熱後に焼成物からスクリーンに等により容易に分
離される程度に存きい粒径をもてばよい。但し、
特に微粉状の固体炭素は本発明における加熱処理
条件下に速やかに一酸化炭素や二酸化炭素に酸化
されるので、処理条件下にこのように酸化される
限りの量であれば、原料混合粉末に一様に混合さ
せてもよく、また、それが望ましい場合もある。 本発明の方法を実施するに当つては、原料混合
粉末の加熱焼成容器として窒素のような非酸化性
ガスの導入管と、排気管とを備えた密閉容器を用
いるのが好都合である。即ち、一つの具体的な方
法として、容器の底部に木炭を層状に敷き、空気
雰囲気下に木炭層上に、酸化亜鉛粉末と酸化ガリ
ウム粉末を収容したるつぼを置き、次に、非酸化
性ガス導入管を閉じ、排気管を開いて、電気炉中
で容器を所定時間、所定温度に加熱する。 本発明においては、空気雰囲気に原料粉末混合
物の加熱焼成を始めても、時間の経過につれて、
固体炭素が雰囲気中の空気と反応して自然に還元
性雰囲気を形成するので、加熱焼成時に水素や一
酸化炭素、或いはこれらと窒素との混合ガスを強
制的に容器内に流通させる必要がない。本発明に
おいては、このように加熱焼成時に還元性ガスが
発生するので、前記したようにこの還元性ガスは
空気と共に排気管から自然に排出させて、容器内
をほぼ一定圧の還元性雰囲気に保つのが望まし
い。 原料混合粉末を所定時間加熱焼成後に冷却する
ときは、容器内を大気と遮断するか、又は容器内
に窒素ガスを流通させ、非酸化性雰囲気下に置く
のが望ましい。焼成物が冷却される過程で空気の
ような酸化性ガスに接触すると、得られる焼成物
の導電性が低下することがあるからである。本発
明においては、200℃以下、好ましくは常温まで、
このように非酸化性雰囲気下に加熱焼成物を冷却
するのが望ましい。但し、冷却方法は自然冷却で
も強制冷却でもよい。 尚、本発明においては、必要に応じて原料混合
粉末はアルミニウム、インジウム、スズ、ニツケ
ル、モリブデン等の金属の酸化物の一種又は二種
以上を含有していてもよく、この場合、その配合
量は、酸化亜鉛に基づいて10重量%以下が好まし
い。 本発明の方法は以上のように、導電性酸化亜鉛
を製造する方法において、酸化亜鉛に導電性を付
与するための活性化剤として酸化ガリウムを用い
ると共に、酸化亜鉛と酸化ガリウムとの混合粉末
を固体炭素の存在下に加熱焼成することにより、
従来は困難であつた平均粒径が1μより小さい導
電性酸化亜鉛微粉末を得ることに成功したもので
あり、好ましい場合には得られる酸化亜鉛は同時
に導電性が著しく改善され、1Ω.cmより小さい
体積固有抵抗を有する。 勿論、本発明の方法によれば、固体炭素を空気
雰囲気下で加熱して還元性ガスを生じさせるか
ら、水素や一酸化炭素ガスを容器内に流通させる
必要もない。 以下に本発明の実施例を挙げるが、本発明はこ
れら実施例に限定されるものではない。 実施例 1 平均粒径0.6μの酸化亜鉛粉末100重量部と平均
粒径1.4μの酸化ガリウムの所定量を試験用小型混
合機「マイクロスピードミキサー」(宝工機製)
にて5分間乾式混合し、原料粉末を調製した。 ステンレス耐熱鋼製容器の底部に荒砕きした木
炭8重量部を層状に敷き、上記原料混合粉末30重
量部を収容したるつぼを木炭層上に置いた後、表
に示す温度に3時間、電気炉中で加熱した。この
間、発生した還元性ガスは容器から自然に排気さ
せた。次に、容器内に緩やかに窒素ガスを流通さ
せつつ、加熱焼成物を室温まで冷却した。得られ
た酸化亜鉛粉末の体積固有抵抗(Ω・cm)及び平
The present invention relates to a method for producing conductive zinc oxide. Conductive zinc oxide has excellent advantages such as its conductivity, oil odor resistance, heat resistance, and light resistance, so it is used for facsimile recording paper and other information recording paper for electrostatic recording, current recording, and discharge recording, and for industrial use. In addition to being used as a coating agent in the production of recording paper, it is also widely used as a conductive agent in synthetic resin films and synthetic fibers. Various methods for producing such conductive zinc oxide are already known. A typical example of these is as disclosed in U.S. Pat. This method involves heating and firing at a temperature of 600 to 900°C. However, since this method uses hydrogen or carbon monoxide as the reducing gas, there is a risk of explosion. To avoid this, the reducing gas must be mixed with an inert gas such as nitrogen and fired in a reducing atmosphere with a predetermined non-explosive composition, which makes process management complicated. In addition, the equipment becomes complicated and the product ends up being expensive. Furthermore, in all conventional methods, zinc oxide and an activator are uniformly kneaded with water to form a slurry or paste, and then this is dried, pulverized, and heated and calcined. Since the raw material tends to sinter and become granular or agglomerated during heating and firing, it is necessary to crush it again after heating and firing, but the resulting zinc oxide powder has a significantly large average particle size. As mentioned above, the conventional method requires complicated process control and a large number of steps, but the conductivity is still not sufficient, and furthermore, due to the large average particle size, it is subject to various restrictions in terms of application. Of course, it is also extremely unsatisfactory economically. In order to solve these various problems, the present inventors have already dry-mixed zinc oxide powder and aluminum oxide powder and heated and fired them in the presence of solid carbon to create an oxide with improved conductivity. We are proposing a method to produce zinc at low cost. (Tokuko Showa 55
−19897). According to this method, the raw material oxides are dry mixed and heated and fired, so the raw material powders do not significantly adhere to each other and agglomerate during the heating and firing stage, and relatively fine conductive zinc oxide powder can be obtained. There is a strong demand for a smaller diameter.
For example, in order to impart conductivity to synthetic fibers, fine powder with an average particle size of 1 μm or less is preferred from the viewpoint of spinnability. however,
In the method of heating zinc oxide and aluminum oxide in the presence of solid carbon, the raw materials must be Mixed powder 900~
It requires firing at a high temperature of 1100℃, and as a result, even if fine aluminum oxide with an average particle size of about 20μ is used, the raw material powder tends to adhere to each other and agglomerate, resulting in an average particle size of 1μ or less. It is difficult to obtain conductive zinc oxide fine powder. On the other hand, the conductivity is also 1Ω. Even improved zinc oxide with a volume resistivity of less than cm is also required, but this appears to be difficult under normal processing conditions as long as aluminum oxide is used. The present invention has been made in order to solve the above-mentioned problems in the conventional method, and has an average particle diameter of less than 1 μm and/or further improved conductivity to achieve a volume resistivity of 1Ω. The purpose of the present invention is to provide a method for producing zinc oxide smaller than cm. The method for producing conductive zinc oxide according to the present invention uses zinc oxide powder and a
It is characterized in that 5 moles of gallium oxide powder are dry mixed and then heated and fired at a temperature of 700 to 1100°C in the presence of solid carbon. In the present invention, the mixing ratio of gallium oxide to zinc oxide is 0.05 to 100 moles of zinc oxide.
-5 mol, preferably 0.1-2.5 mol. When the mixing ratio of gallium oxide is less than the above range, the zinc oxide obtained by heating and firing will not have high conductivity, and on the other hand, it is economically disadvantageous to use a larger amount than the above range. The method of the invention has two aspects. One aspect relates to the average particle size of the resulting zinc oxide, and the other aspect relates to the volume resistivity of the resulting zinc oxide.
Although the present invention is not limited to this, as the heating and firing temperature of the raw material mixed powder of zinc oxide powder and gallium oxide powder increases, the volume resistivity of the resulting conductive zinc oxide decreases, but on the other hand, the average A tendency for the particle size to increase is observed. Furthermore, if the heating and firing temperature of the raw material mixture is fixed, the volume resistivity of the resulting conductive zinc oxide tends to decrease as the ratio of gallium oxide to zinc oxide increases. Therefore, according to the method of the present invention, in a preferred case, the average particle size is smaller than 1μ and the volume resistivity is 1Ω. Highly conductive zinc oxide fine powder smaller than cm is obtained. Furthermore, if necessary, by heating and firing the raw material powder at a high temperature, a highly conductive zinc oxide powder having a significantly small volume resistivity can be obtained at the expense of some average particle size. In the present invention, in order to obtain conductive zinc oxide having an average particle size of less than 1 μm, the average particle size of the zinc oxide used must be less than 1 μm, and preferably
It is 0.1-0.8μ. Since the amount of gallium oxide powder mixed with zinc oxide is small, the average particle size is a few microns.
It may be less than or equal to 2 μm, and gallium oxide powder of 2 μ or less is usually preferably used. The heating and firing temperature must be relatively low, especially at temperatures above 700°C and 900°C.
A temperature range below 0.degree. C. is preferred. When zinc oxide and gallium oxide are heated and calcined in the presence of solid carbon under these conditions, a conductive zinc oxide powder with an average particle size of less than 1μ is obtained, preferably an average particle size of 0.7-0.8μ. Moreover, the volume resistivity is also 1Ω. Highly conductive zinc oxide fine powder smaller than cm is obtained. When fired at a high temperature of 900° C. or higher, the raw material powders tend to adhere to each other and agglomerate, so the resulting conductive zinc oxide has an average particle size of 2 to 3 μm. However, regardless of the average particle size of the conductive zinc oxide powder obtained, if the purpose is to improve the conductivity, the average particle size of the zinc oxide powder and gallium oxide powder used is not particularly limited, and the raw material mixture powder
It is preferable to heat and bake at a high temperature in the range of 850 to 1100°C, preferably 900 to 1100°C in view of the amount of gallium oxide used. By treatment under such conditions, highly conductive zinc oxide powder having a volume resistivity of less than 1 Ω·cm can be obtained. As mentioned above, conductive zinc oxide fine powder with an average particle size of less than 1 μm can be obtained by heating and firing at a low temperature of 800°C or less, but on the other hand, its volume resistivity is several Ω·cm to several Ω·cm. Ten ohms. cm and 1Ω.
This is because it is difficult to make the size smaller than cm. In both aspects of the present invention,
Heating to a high temperature exceeding 1100° C. is not preferable because the formation of metallic zinc becomes noticeable and the yield of the desired conductive zinc oxide decreases. Further, in the present invention, a gallium compound capable of producing gallium oxide under the processing conditions can be used in place of or together with gallium oxide, if necessary. To dry mix zinc oxide powder and gallium oxide powder, for example, a rotating container type mixer such as a V-type mixer, a ribbon type, screw type, rotary blade type, or other fixed container type mixer is used as appropriate. be able to. The mixing method is not particularly limited as long as the zinc oxide powder and the gallium oxide powder can be dry mixed uniformly. Further, the heating and baking time is usually about 15 minutes to 5 hours. As the solid carbon, for example, powdered, granular or lump charcoal is suitable. Such solid carbon is separated from or mixed with the raw material mixed powder of zinc oxide and gallium oxide, and heated together with the mixed powder in a container. When solid carbon is mixed with the raw material mixed powder and heated, it is sufficient that the carbon has a particle size large enough to be easily separated from the fired product using a screen or the like after heating the raw material mixed powder. however,
In particular, fine powder solid carbon is rapidly oxidized to carbon monoxide and carbon dioxide under the heat treatment conditions of the present invention, so if the amount is oxidized in this way under the treatment conditions, it can be added to the raw material mixed powder. Uniform mixing may be possible and may be desirable. In carrying out the method of the present invention, it is convenient to use a closed container equipped with an inlet pipe for a non-oxidizing gas such as nitrogen and an exhaust pipe as the container for heating and firing the raw material mixed powder. That is, one specific method is to lay a layer of charcoal on the bottom of a container, place a crucible containing zinc oxide powder and gallium oxide powder on the charcoal layer in an air atmosphere, and then pour a non-oxidizing gas The inlet pipe is closed, the exhaust pipe is opened, and the container is heated to a predetermined temperature for a predetermined time in an electric furnace. In the present invention, even if heating and baking of the raw material powder mixture is started in an air atmosphere, as time passes,
Since solid carbon reacts with the air in the atmosphere to naturally form a reducing atmosphere, there is no need to force hydrogen, carbon monoxide, or a mixed gas of these and nitrogen into the container during heating and firing. . In the present invention, reducing gas is generated during heating and firing, so as mentioned above, this reducing gas is naturally discharged from the exhaust pipe along with the air to create a reducing atmosphere in the container at an approximately constant pressure. It is desirable to keep it. When cooling the raw material mixed powder after heating and firing for a predetermined period of time, it is desirable to isolate the inside of the container from the atmosphere or to circulate nitrogen gas in the container to place it in a non-oxidizing atmosphere. This is because if the fired product comes into contact with an oxidizing gas such as air during the cooling process, the conductivity of the resulting fired product may decrease. In the present invention, up to 200°C or lower, preferably at room temperature,
It is desirable to cool the heated and fired product under a non-oxidizing atmosphere in this manner. However, the cooling method may be natural cooling or forced cooling. In addition, in the present invention, the raw material mixed powder may contain one or more kinds of oxides of metals such as aluminum, indium, tin, nickel, and molybdenum, if necessary, and in this case, the blended amount is preferably 10% by weight or less based on zinc oxide. As described above, the method of the present invention is a method for producing conductive zinc oxide, in which gallium oxide is used as an activator to impart conductivity to zinc oxide, and a mixed powder of zinc oxide and gallium oxide is used. By heating and firing in the presence of solid carbon,
We have succeeded in obtaining conductive zinc oxide fine powder with an average particle size of less than 1μ, which was previously difficult, and in favorable cases, the resulting zinc oxide has significantly improved conductivity, reaching 1Ω. It has a volume resistivity smaller than cm. Of course, according to the method of the present invention, solid carbon is heated in an air atmosphere to generate a reducing gas, so there is no need to circulate hydrogen or carbon monoxide gas into the container. Examples of the present invention are listed below, but the present invention is not limited to these Examples. Example 1 100 parts by weight of zinc oxide powder with an average particle size of 0.6μ and a predetermined amount of gallium oxide with an average particle size of 1.4μ were mixed using a small mixing machine "Micro Speed Mixer" (manufactured by Takara Koki) for testing.
The mixture was dry mixed for 5 minutes to prepare a raw material powder. 8 parts by weight of coarsely crushed charcoal was spread in a layer at the bottom of a heat-resistant stainless steel container, and a crucible containing 30 parts by weight of the above raw material mixed powder was placed on the charcoal layer, then heated in an electric furnace at the temperature shown in the table for 3 hours. It was heated inside. During this time, the reducing gas generated was allowed to vent naturally from the container. Next, the heated and fired product was cooled to room temperature while nitrogen gas was slowly passed through the container. Volume resistivity (Ω・cm) and average of the obtained zinc oxide powder

【表】 均粒径(μ)を表に示す。 また、上記の導電性酸化亜鉛粉末の白色度JIS
8123)は80であつて、次の比較例で得た酸化亜鉛
粉末に比べて白色度も改善されていることが認め
られた。 比較例 実施例と同じ酸化亜鉛粉末100重量部と平均粒
径20mμの酸化アルミニウムとを実施例と同様に
乾式混合した後、1010℃の温度で2.5時間焼成し
た。このようにして得られた導電性酸化亜鉛は体
積固有抵抗60Ω・cm、平均粒径14.3μであつた。
また、ハンター白色度は78.8であり、やや灰色を
帯びていた。
[Table] The average particle diameter (μ) is shown in the table. In addition, the whiteness of the above conductive zinc oxide powder JIS
8123) was 80, and it was recognized that the whiteness was also improved compared to the zinc oxide powder obtained in the following comparative example. Comparative Example 100 parts by weight of the same zinc oxide powder as in the example and aluminum oxide having an average particle size of 20 mμ were dry mixed in the same manner as in the example, and then fired at a temperature of 1010° C. for 2.5 hours. The conductive zinc oxide thus obtained had a volume resistivity of 60 Ω·cm and an average particle size of 14.3 μm.
In addition, the Hunter whiteness was 78.8, which was slightly grayish.

Claims (1)

【特許請求の範囲】 1 酸化亜鉛粉末と、酸化亜鉛100モルに対して
0.05〜5モルの酸化ガリウム粉末を乾式混合し、
固体炭素の存在下に700〜1100℃の温度に加熱焼
成することを特徴とする導電性酸化亜鉛の製造方
法。 2 加熱焼成を700℃以上で900℃より低い温度で
行なつて、平均粒径が1μより小さい酸化亜鉛粉
末を得ることを特徴とする特許請求の範囲第1項
記載の導電性酸化亜鉛の製造方法。 3 加熱焼成後、非酸化性雰囲気下で200℃以下
の温度に冷却することを特徴とする特許請求の範
囲第1項記載の導電性亜鉛の製造方法。
[Claims] 1. Zinc oxide powder and 100 moles of zinc oxide
Dry mixing 0.05 to 5 moles of gallium oxide powder,
A method for producing conductive zinc oxide, which comprises heating and firing at a temperature of 700 to 1100°C in the presence of solid carbon. 2. Production of conductive zinc oxide according to claim 1, characterized in that heating and firing is performed at a temperature of 700°C or higher and lower than 900°C to obtain zinc oxide powder having an average particle size of less than 1μ. Method. 3. The method for producing conductive zinc according to claim 1, which comprises cooling to a temperature of 200° C. or lower in a non-oxidizing atmosphere after heating and baking.
JP2944682A 1982-02-24 1982-02-24 Preparation of electrically-conductive zinc oxide Granted JPS58145620A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2944682A JPS58145620A (en) 1982-02-24 1982-02-24 Preparation of electrically-conductive zinc oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2944682A JPS58145620A (en) 1982-02-24 1982-02-24 Preparation of electrically-conductive zinc oxide

Publications (2)

Publication Number Publication Date
JPS58145620A JPS58145620A (en) 1983-08-30
JPH0212883B2 true JPH0212883B2 (en) 1990-03-29

Family

ID=12276341

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2944682A Granted JPS58145620A (en) 1982-02-24 1982-02-24 Preparation of electrically-conductive zinc oxide

Country Status (1)

Country Link
JP (1) JPS58145620A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4526861B2 (en) * 2004-04-23 2010-08-18 出光興産株式会社 Zinc based complex oxide
CN117654471A (en) * 2023-11-30 2024-03-08 联瑞新材(连云港)有限公司 A kind of spherical zinc oxide powder and preparation method thereof

Also Published As

Publication number Publication date
JPS58145620A (en) 1983-08-30

Similar Documents

Publication Publication Date Title
US4117096A (en) Process for producing powder of β-type silicon carbide
JPS5850929B2 (en) Method for manufacturing silicon carbide powder
JPS6156170B2 (en)
JPS6332747B2 (en)
JPH0212883B2 (en)
JPH0513089B2 (en)
JPS599506B2 (en) Method for producing conductive zinc oxide
CN102211937B (en) Method for synthesizing high-purity aluminum silicon carbon superfine powder
US4500644A (en) Preparation and composition of sialon grain and powder
US5011798A (en) Chromium additive and method for producing chromium alloy using the same
JPS6126550A (en) Manufacture of refractories containing gllasified material
JPH0118005B2 (en)
US2170814A (en) Method of preparing copper powder
US3533781A (en) Process for producing dispersion hardened nickel
JPS5891019A (en) Manufacture of aluminum nitride-base powder
US2217569A (en) Process for the production of metallic iron powder
JP5073262B2 (en) Friction material containing composite titanic acid compound and powder thereof
CN112251600A (en) Preparation method and application of chromium metallization ball
JP3333547B2 (en) γ-lithium aluminate and method for producing the same
RU2344105C2 (en) Carbon-bearing fire-resistant material and method of production thereof
JPS62146229A (en) Production of metal matrix composite material
JPS5997531A (en) Manufacture of electrically conductive white filler
JPH05279002A (en) Production of al nitride powder
JPS63225506A (en) Production of aluminum nitride powder
JPS58217469A (en) Manufacture of silicon nitride-silicon carbide composition