JPS63147823A - Production of zinc oxide fine particle - Google Patents

Production of zinc oxide fine particle

Info

Publication number
JPS63147823A
JPS63147823A JP29475286A JP29475286A JPS63147823A JP S63147823 A JPS63147823 A JP S63147823A JP 29475286 A JP29475286 A JP 29475286A JP 29475286 A JP29475286 A JP 29475286A JP S63147823 A JPS63147823 A JP S63147823A
Authority
JP
Japan
Prior art keywords
gas
zinc oxide
zinc
inert gas
vapor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP29475286A
Other languages
Japanese (ja)
Inventor
Tsuneo Funahashi
舟橋 恒男
Shinji Ezaki
江崎 慎二
Takayuki Hashimoto
橋本 高幸
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP29475286A priority Critical patent/JPS63147823A/en
Publication of JPS63147823A publication Critical patent/JPS63147823A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To enlarge a specific surface area of the titled particle and to reduce the contained excess Zn by oxidizing and combusting a vapor of metallic Zn together with a jet gas contg. a combustible gas of a specified proportion in an oxidizing atmosphere. CONSTITUTION:The jet gas is obtained by allowing at inert gas as a carrier gas to contain 3-30vol% combustible gas (to the inert gas). The vapor of metallic Zn is allowed to blow out together with the jet gas into the atmosphere contg. O2. Then the above-mentioned metallic Zn is oxidized and combusted and the obtained oxidized Zn is rapidly cooled.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、比表面積が大きく、かつ、過剰亜鉛が少ない
酸化亜鉛微粒子の製造方法の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an improvement in a method for producing zinc oxide fine particles having a large specific surface area and a small amount of excess zinc.

(従来の技術〕 酸化亜鉛粒子は、広い用途を有する工業製品で、例えば
、ゴムの加硫促進剤、塗料、触媒、医薬品、電子写真用
感光材料、ファンデーション、クリーム等の化粧品、バ
リスター、フェライト等の電子部品材料などに用いられ
ている。
(Prior Art) Zinc oxide particles are industrial products with a wide range of uses, such as rubber vulcanization accelerators, paints, catalysts, pharmaceuticals, electrophotographic materials, foundations, cosmetics such as creams, varistors, and ferrites. It is used in electronic component materials such as

このような用途に用いられる酸化亜鉛はできるだけ微粒
であること、即ち粒子の比表面積が大きいこと、及びそ
の純度が高いことが必要である。
Zinc oxide used for such purposes needs to be as fine as possible, that is, the particles need to have a large specific surface area and have high purity.

従来、酸化亜鉛の製造方法としては次に述べる乾式法が
知られている。即ち、この方法は、酸素を含有する雰囲
気中に金属亜鉛蒸気をキャリアガスとしての不活性ガス
と共に噴出させて導入して金属亜鉛を酸化燃焼させ、得
られた酸化亜鉛を急冷するというものである。
Conventionally, the following dry method is known as a method for producing zinc oxide. That is, in this method, metallic zinc vapor is jetted and introduced together with an inert gas as a carrier gas into an oxygen-containing atmosphere to oxidize and burn metallic zinc, and the obtained zinc oxide is rapidly cooled. .

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、上記方法によって得られる酸化亜鉛の粒子は、
比表面積が15m/gより小さく、また、含有される過
剰亜鉛が重量にてl OOppmより大きいために、粒
度においても純度においても充分満足し得るものではな
かった。
However, the zinc oxide particles obtained by the above method are
Since the specific surface area was less than 15 m/g and the excess zinc contained was greater than 100 ppm by weight, the particle size and purity were not fully satisfactory.

本発明の目的は、このような従来の方法を改良して、こ
の方法の問題点を解決し、比表面積が15m/g以上で
、含有される過剰亜鉛が重量にて100 ppm以下の
酸化亜鉛微粒子を製造し得る方法を提供することにある
The purpose of the present invention is to improve such conventional methods, solve the problems of this method, and produce zinc oxide having a specific surface area of 15 m/g or more and containing excess zinc of 100 ppm or less by weight. The object of the present invention is to provide a method for producing fine particles.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、前記問題点を解決するものとして、酸素を含
有する雰囲気中に金属亜鉛蒸気をキャリアガスとしての
不活性ガスと共に噴出させて金属亜鉛を酸化燃焼させ、
得られた酸化亜鉛を急冷する方法において、該噴出ガス
に不活性ガス量の3〜30容■%の可燃性ガスを含有さ
せることを特徴とするものである。
The present invention solves the above-mentioned problems by oxidizing and burning metal zinc by spouting metal zinc vapor together with an inert gas as a carrier gas into an oxygen-containing atmosphere.
The method for rapidly cooling the obtained zinc oxide is characterized in that the ejected gas contains combustible gas in an amount of 3 to 30% by volume based on the amount of inert gas.

〔作 用〕[For production]

金属亜鉛を加熱して蒸発させて得られた金属亜鉛蒸気は
ノズルからキャリアガスとして窒素、アルゴン等の不活
性ガスと共に燃焼室へ噴出する。
Metal zinc vapor obtained by heating and evaporating metal zinc is ejected from a nozzle into a combustion chamber as a carrier gas together with an inert gas such as nitrogen or argon.

燃焼室の雰囲気は酸素を含有するものであり、空気又は
酸素を前記ノズルとは別のノズルより供給する。このよ
うな雰囲気中に噴出された前記金属亜鉛蒸気は直ちに酸
化燃焼して酸化亜鉛を生成する。生成した酸化亜鉛は冷
却するまでに団塊状粒子に焼結するのを抑制するため急
冷した後、捕集される。
The atmosphere in the combustion chamber contains oxygen, and air or oxygen is supplied from a nozzle different from the above-mentioned nozzle. The metallic zinc vapor ejected into such an atmosphere is immediately oxidized and burned to produce zinc oxide. The generated zinc oxide is rapidly cooled to prevent it from sintering into nodular particles before being cooled, and then collected.

本発明においては、前記燃焼室に噴出される金属亜鉛蒸
気および不活性ガスに更に該不活性ガス量の3〜30容
量%の可燃性ガスを含有させる。
In the present invention, the metal zinc vapor and inert gas ejected into the combustion chamber further contain 3 to 30% by volume of combustible gas based on the amount of inert gas.

可燃性ガスとしては、周知の水素、−酸化炭素、プロパ
ン等が挙げられる。この不活性ガスを含有させないと、
本発明の目的である比表面積および過剰亜鉛の条件のう
ち高々、いずれか1つしか達成され得ない場合が多くな
る。含有させる量が不活性ガス量の3容量%未満では上
記可燃性ガスを含有させる効果が稀薄となり、また、3
0容量%を超えると酸化亜鉛が生成する際の燃焼温度が
高すぎて、生成する粒子の比表面積が小さくなる。
Examples of the combustible gas include well-known hydrogen, carbon oxide, propane, and the like. If this inert gas is not included,
There are many cases where at most only one of the specific surface area and excess zinc conditions, which are the objectives of the present invention, can be achieved. If the amount to be contained is less than 3% by volume of the inert gas amount, the effect of containing the above-mentioned flammable gas will be diluted, and
If it exceeds 0% by volume, the combustion temperature when zinc oxide is produced is too high, and the specific surface area of the particles produced becomes small.

このように可燃性ガスを含有させることにより比表面積
および過剰亜鉛のいずれの条件をも満足させ得るのは、
酸化亜鉛が生成する際の燃焼温度および生成した酸化亜
鉛が燃焼域で滞留している時間が、可燃性ガスを含有さ
せなかった場合に比べて、夫々より高温に、より短時間
になったことによるものと推察される。
The reason why both the specific surface area and excess zinc conditions can be satisfied by containing a flammable gas is as follows.
The combustion temperature when zinc oxide is generated and the time that the generated zinc oxide stays in the combustion zone are higher and shorter, respectively, than when no flammable gas is included. It is assumed that this is due to the following.

なお、噴出されるガスのうち、可燃性ガス以外の金属亜
鉛蒸気および不活性ガスの量については、夫々7〜25
g/分、8〜20!!/分程度が好ましい。
In addition, the amount of metal zinc vapor and inert gas other than combustible gas among the ejected gases is 7 to 25%, respectively.
g/min, 8-20! ! /minute is preferable.

このような乾式法で得られた微粒で純度の高い酸化亜鉛
粒子は、電子写真用感光材料として好適である。また、
ノビが良いことや皮層の紫外線防御等に好適である点で
、ファンデーション、日焼は止めクリーム等の化粧品の
原料としても最適である。
Fine and highly pure zinc oxide particles obtained by such a dry method are suitable as a light-sensitive material for electrophotography. Also,
It is also ideal as a raw material for cosmetics such as foundations and sunscreen creams because of its good elasticity and its ability to protect the skin from UV rays.

〔実施例〕〔Example〕

以下、本発明を実施例および比較例によって具体的に説
明する。
Hereinafter, the present invention will be specifically explained using Examples and Comparative Examples.

実施例1 第1図は本発明方法の実施に用いた装置の概略図である
。図において、燃焼室1は、抵抗発熱体を取り付けた電
気炉2の上に断熱レンガにより内部を一辺50cmの立
方体状に形成した。電気炉2には、上部に金属亜鉛蒸気
を噴出するノズル3を有する黒鉛ルツボ4が載置される
。この黒鉛ルツボ4内に装入された金属亜鉛(純度99
.99重量%)が、電気炉2により加熱され溶解される
。溶解した金属亜鉛浴面上にキャリアガスとしての窒素
もしくはこの窒素と可燃性ガス(水素、−酸化炭素およ
びプロパン)を導入することができる導入管5が、黒鉛
ルツボ4に設けられている。前記ノズル3の周囲には、
燃焼室1内を酸素を含有する雰囲気に維持するために旋
回流の酸素を吹き込むための風箱6が、また、ノズル3
付近で着火して生じたフレームの直上には、生成した酸
化亜鉛を急冷するための冷却用空気吹込管7が設けであ
る。
Example 1 FIG. 1 is a schematic diagram of an apparatus used to carry out the method of the present invention. In the figure, a combustion chamber 1 was formed in the shape of a cube with a side of 50 cm using insulating bricks on an electric furnace 2 equipped with a resistance heating element. A graphite crucible 4 is placed in the electric furnace 2 and has a nozzle 3 at the top for spouting metallic zinc vapor. Metal zinc (purity 99
.. 99% by weight) is heated and melted in the electric furnace 2. The graphite crucible 4 is provided with an inlet pipe 5 through which nitrogen as a carrier gas or nitrogen and a combustible gas (hydrogen, -carbon oxide and propane) can be introduced onto the surface of the melted metal zinc bath. Around the nozzle 3,
A wind box 6 for blowing a swirling flow of oxygen in order to maintain an oxygen-containing atmosphere inside the combustion chamber 1 is also connected to a nozzle 3.
A cooling air blowing pipe 7 for rapidly cooling the produced zinc oxide is installed directly above the flame that is ignited nearby.

燃焼室1の出口8は、グーズネソク煙道9、分級ボック
ス10、捕集装置を介して吸引ファンに接続している(
捕集装置と吸引ファンは図示せず)。
The outlet 8 of the combustion chamber 1 is connected to a suction fan via a gas flue 9, a classification box 10, and a collection device (
(Collection device and suction fan not shown).

第1図の装置によって、金属亜鉛を10kg溶解し、風
箱6より酸素を507!/分吹き込み、冷却用空気吹込
管7より空気を167n/分吹き込むことによって酸化
亜鉛を製造する実験を行なった。
Using the apparatus shown in Figure 1, 10 kg of metallic zinc is melted, and 507 kg of oxygen is added from the wind box 6! An experiment was conducted to produce zinc oxide by blowing air at 167 n/min from the cooling air blowing pipe 7.

その他の酸化亜鉛製造条件および実験により得られた酸
化亜鉛の品質特性を第1表に示す。
Other zinc oxide production conditions and quality characteristics of zinc oxide obtained through experiments are shown in Table 1.

〔発明の効果〕〔Effect of the invention〕

以上から明らかなように、本発明方法によれば、乾式法
により比表面積が15m/g以上で、含有される過剰亜
鉛が重量にて100 ppm以下の醇化亜鉛微粒子を製
造することができ、この方法は工業的実用性の高いもの
である。
As is clear from the above, according to the method of the present invention, zinc fertilized fine particles having a specific surface area of 15 m/g or more and containing 100 ppm or less of excess zinc by weight can be produced by a dry method. The method has high industrial practicality.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例に用いた実験装置の概略図であ
る。
FIG. 1 is a schematic diagram of an experimental apparatus used in an example of the present invention.

Claims (1)

【特許請求の範囲】[Claims] (1)酸素を含有する雰囲気中に金属亜鉛蒸気をキャリ
アガスとしての不活性ガスと共に噴出させて金属亜鉛を
酸化燃焼させ、得られた酸化亜鉛を急冷する方法におい
て、該噴出ガスに不活性ガス量の3〜30容量%の可燃
性ガスを含有させることを特徴とする酸化亜鉛微粒子の
製造方法。
(1) In a method in which metal zinc vapor is ejected together with an inert gas as a carrier gas into an oxygen-containing atmosphere to oxidize and burn the metal zinc, and the resulting zinc oxide is rapidly cooled, the ejected gas is mixed with an inert gas. A method for producing zinc oxide fine particles, which comprises containing combustible gas in an amount of 3 to 30% by volume.
JP29475286A 1986-12-12 1986-12-12 Production of zinc oxide fine particle Pending JPS63147823A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29475286A JPS63147823A (en) 1986-12-12 1986-12-12 Production of zinc oxide fine particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29475286A JPS63147823A (en) 1986-12-12 1986-12-12 Production of zinc oxide fine particle

Publications (1)

Publication Number Publication Date
JPS63147823A true JPS63147823A (en) 1988-06-20

Family

ID=17811844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29475286A Pending JPS63147823A (en) 1986-12-12 1986-12-12 Production of zinc oxide fine particle

Country Status (1)

Country Link
JP (1) JPS63147823A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007161580A (en) * 2005-12-16 2007-06-28 Degussa Gmbh Method for producing zinc oxide powder
JP2009545509A (en) * 2006-08-17 2009-12-24 エボニック デグサ ゲーエムベーハー Silica coated zinc oxide particles obtained by flame pyrolysis method
JP2013001578A (en) * 2011-06-13 2013-01-07 Sakai Chem Ind Co Ltd Zinc oxide, method for producing zinc oxide, cosmetic, coating composition, and resin composition
CN109415627A (en) * 2016-06-30 2019-03-01 堺化学工业株式会社 Zinc oxide fluorophor and its manufacturing method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007161580A (en) * 2005-12-16 2007-06-28 Degussa Gmbh Method for producing zinc oxide powder
EP1820778A2 (en) * 2005-12-16 2007-08-22 Degussa GmbH Process for the making zinc oxide powder
EP1820778A3 (en) * 2005-12-16 2008-04-02 Evonik Degussa GmbH Process for the making zinc oxide powder
JP4571932B2 (en) * 2005-12-16 2010-10-27 エボニック デグサ ゲーエムベーハー Production method of zinc oxide powder
JP2009545509A (en) * 2006-08-17 2009-12-24 エボニック デグサ ゲーエムベーハー Silica coated zinc oxide particles obtained by flame pyrolysis method
JP2013001578A (en) * 2011-06-13 2013-01-07 Sakai Chem Ind Co Ltd Zinc oxide, method for producing zinc oxide, cosmetic, coating composition, and resin composition
CN109415627A (en) * 2016-06-30 2019-03-01 堺化学工业株式会社 Zinc oxide fluorophor and its manufacturing method
US11312902B2 (en) 2016-06-30 2022-04-26 Sakai Chemical Industry Co., Ltd. Zinc oxide phosphor and method for producing same

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