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JPS6029645B2 - Method for producing acicular zinc oxide particles - Google Patents

Method for producing acicular zinc oxide particles

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Publication number
JPS6029645B2
JPS6029645B2 JP9122681A JP9122681A JPS6029645B2 JP S6029645 B2 JPS6029645 B2 JP S6029645B2 JP 9122681 A JP9122681 A JP 9122681A JP 9122681 A JP9122681 A JP 9122681A JP S6029645 B2 JPS6029645 B2 JP S6029645B2
Authority
JP
Japan
Prior art keywords
zinc
particle size
zinc oxide
oxide particles
moles
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
JP9122681A
Other languages
Japanese (ja)
Other versions
JPS57205320A (en
Inventor
一美 藤田
恵三 松田
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.)
Tokai University
Original Assignee
Tokai University
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 Tokai University filed Critical Tokai University
Priority to JP9122681A priority Critical patent/JPS6029645B2/en
Publication of JPS57205320A publication Critical patent/JPS57205320A/en
Publication of JPS6029645B2 publication Critical patent/JPS6029645B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は針状酸化亜鉛粒子の生成法に関し、特に均一な
粒子径を有する針状酸化亜鉛粒子の生成法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing acicular zinc oxide particles, and particularly to a method for producing acicular zinc oxide particles having a uniform particle size.

従来、針状酸化亜鉛を生成する方法としては金属亜鉛の
加熱により生ずる亜鉛蒸気を酸化する方法が用し、らて
し、たが、この方法では高温で処理するため加熱条件を
一定に保つことはむずかしく、得られた粒子同志が焼絹
をおこし、粒子の形状や粒度を一定に保つことは困難で
あった。
Conventionally, the method for producing acicular zinc oxide was to oxidize the zinc vapor produced by heating metal zinc.However, this method requires the heating conditions to be kept constant because the process is carried out at high temperatures. However, it was difficult to keep the shape and size of the particles constant, as the resulting particles would cause burnt silk.

このため粒子の性状が微妙な影響を与える触媒への用途
が限られる等の欠点があった。また高温装道やキャリア
ガス等を必要とするので、その装置も複雑で高価なもの
となる欠点もあった。本発明はこれらの問題点を解決す
ることを目的としてなされたもので、従来のものに比し
て均一な粒子径を持つ針状酸化亜鉛粒子を水溶液中で生
成し、かつ反応条件によりその粒子径を制御できる針状
酸化亜鉛粒子の生成法を提供するものである。
For this reason, there have been drawbacks such as limited application to catalysts where particle properties have a subtle effect. Furthermore, since high-temperature equipment, carrier gas, etc. are required, the device also has the disadvantage of being complicated and expensive. The present invention was made with the aim of solving these problems, and it is possible to produce acicular zinc oxide particles in an aqueous solution with a uniform particle size compared to conventional ones, and to change the particle size by adjusting the reaction conditions. The present invention provides a method for producing acicular zinc oxide particles whose diameter can be controlled.

即ち、亜鉛塩水溶液に、加水分解により塩基を生成する
有機化合物を添加し、または亜鉛酸塩水溶液に、加水分
解により酸を生成する有機化合物を添加し、針状酸化亜
鉛粒子を得るものである。
That is, acicular zinc oxide particles are obtained by adding an organic compound that generates a base through hydrolysis to an aqueous zinc salt solution, or adding an organic compound that generates an acid through hydrolysis to an aqueous zinc salt solution. .

この反応の概略を示せば次のようである。即ち、亜鉛塩
水溶液に、加水分解により塩基を生成する有機化合物を
添加し、加熱すると加水分解がすすみ、塩基が徐々に亜
鉛塩水溶液中に均一に生成される。
The outline of this reaction is as follows. That is, when an organic compound that generates a base upon hydrolysis is added to an aqueous zinc salt solution and heated, hydrolysis proceeds, and the base is gradually and uniformly generated in the aqueous zinc salt solution.

この生成された塩基が亜鉛塩と反応して酸化亜鉛を生成
する。また、亜鉛酸塩水溶液に、加水分解により酸を生
成する有機化合物を添加し、加熱すると加水分解がすす
み、酸が徐々に亜鉛酸塩水溶液中に均一に生成される。
この生成された酸が亜鉛酸塩と反応して酸化亜鉛を生成
する。ここで用いられる、加水分解により塩基を生成す
る有機化合物としては、加水分解により徐々に塩基を生
成する有機化合物で、かつ水溶性で反応後容易に除去で
きるものならばよい。特に窒素原子を有する有機化合物
を使用することができ、中でもへキサメチレンテトラミ
ンは特に好結果をもたらすものである。この他尿素を用
いることもできる。また、ここで用いられる、加水分解
により酸を生成する有機化合物としては、加水分解によ
り徐々に酸を生成する有機化合物で、かつ水溶性で反応
後容易に除去できるものならばよい。
This generated base reacts with the zinc salt to produce zinc oxide. Furthermore, when an organic compound that generates an acid upon hydrolysis is added to an aqueous zincate solution and heated, hydrolysis proceeds, and the acid is gradually and uniformly generated in the aqueous zincate solution.
This generated acid reacts with zincate to form zinc oxide. The organic compound used here that generates a base upon hydrolysis may be any organic compound that gradually generates a base upon hydrolysis, is water-soluble, and can be easily removed after the reaction. In particular, organic compounds containing nitrogen atoms can be used, among which hexamethylenetetramine gives particularly good results. In addition to this, urea can also be used. Further, the organic compound used here that generates an acid upon hydrolysis may be any organic compound that gradually generates an acid upon hydrolysis, is water-soluble, and can be easily removed after the reaction.

特にェステルを使用することができ、中でもエチレンク
ロルヒドリンは特に好結果をもたらすものである。この
他酢酸エチルを用いることもできる。
In particular, esters can be used, of which ethylene chlorohydrin gives particularly good results. Besides, ethyl acetate can also be used.

反応温度としては20oo〜10000で、より好まし
くはへキサメチレンテトラミンを用いた場合には60o
o〜10000、またエチレンクロルヒドリンを用いた
場合には4000〜10000である。
The reaction temperature is 2000 to 10000, more preferably 6000 when hexamethylenetetramine is used.
o to 10,000, or 4,000 to 10,000 when ethylene chlorohydrin is used.

20qo以下では反応が極端に遅くなり粒子径の制御も
困難となる。
If it is less than 20 qo, the reaction will be extremely slow and it will be difficult to control the particle size.

反応温度と生成粒子径及び粒度分布との関係は、一般に
反応温度が高いほど粒子径は小さくなり、粒度分布は狭
くなる傾向がある。反応時間としては5分〜成分で、よ
り好ましくは6び分である。
Regarding the relationship between the reaction temperature and the particle size and particle size distribution, generally speaking, the higher the reaction temperature, the smaller the particle size and the narrower the particle size distribution. The reaction time is between 5 minutes and more preferably 6 minutes.

5分以下では十分に反応がすすます沈澱も生じない。If the reaction time is 5 minutes or less, the reaction will proceed sufficiently and no precipitation will occur.

また60分以上反応を続けてもこれ以上沈澱は生じない
。亜鉛塩と加水分解により塩基を生ずる有機化合物との
モル比または亜鉛酸塩と加水分解により酸を生ずる有機
化合物とのモル比は使用する亜鉛塩または亜鉛酸塩の種
類によって異るが、モル比と生成粒子径及び粒度分布と
の関係は、一般にはモル比が大きいほど粒子径は小さく
なり、粒度分布は狭くなる傾向がある。反応温度、モル
比等の反応条件を変えることにより、長軸が0.1〜1
5仏m程度の範囲の所望の針状酸化亜鉛粒子を得ること
ができる。
Furthermore, no further precipitation occurs even if the reaction is continued for 60 minutes or more. The molar ratio between the zinc salt and the organic compound that produces a base upon hydrolysis, or the molar ratio between the zinc salt and the organic compound that yields an acid upon hydrolysis, varies depending on the type of zinc salt or zincate used, but the molar ratio In general, the larger the molar ratio, the smaller the particle size and the narrower the particle size distribution. By changing reaction conditions such as reaction temperature and molar ratio, the long axis can be adjusted to 0.1 to 1.
Desired acicular zinc oxide particles having a size of about 5 mm can be obtained.

反応方法は以下のようである。The reaction method is as follows.

即ち、水溶液中で、亜鉛塩と加水分解により塩基を生ず
る有機化合物、または亜鉛酸塩と加水分解により酸を生
ずる有機化合物とを所定温度で所定時間反応させ、生成
した沈澱を櫨過し、水で洗浄し、乾燥させ、さらにその
白色粉末を得ることができる。
That is, in an aqueous solution, a zinc salt and an organic compound that produces a base when hydrolyzed, or a zinc salt and an organic compound that produces an acid when hydrolyzed are reacted at a predetermined temperature for a predetermined period of time, and the resulting precipitate is filtered and dissolved in water. The white powder can be obtained by washing and drying.

この白色粉末は1000qoまで熱的に安定であり、か
つX線回折法により酸化亜鉛であることが確かめられる
This white powder is thermally stable up to 1000 qo, and is confirmed to be zinc oxide by X-ray diffraction.

またその電子顕微鏡写真により、均一な粒子径をもつ針
状粒子であることが確認される。プロピレンを酸化して
ベンゼンを合成する反応の触媒として、本発明で得られ
た針状酸化亜鉛を使用したところ、ベンゼンの選択率が
40%以上にも達し、他の形状の酸化亜鉛を触媒として
使用した場合、例えば球状酸化亜鉛の選択率が約10%
、板状酸化亜鉛の選択率が約5%であるのに比べて高い
触媒能を示した。
Furthermore, the electron micrograph confirms that the particles are acicular particles with a uniform particle size. When the acicular zinc oxide obtained in the present invention was used as a catalyst for the reaction of propylene oxidation to synthesize benzene, the benzene selectivity reached over 40%. When used, for example, the selectivity of spherical zinc oxide is about 10%.
, showed a high catalytic ability compared to the selectivity of plate zinc oxide, which was about 5%.

本発明では直接塩基または酸を添加することなく、加水
分解によって塩基または酸を生ずる有機化合物の存在下
で反応を行っているので、塩基または酸が水溶液中に生
成するのに伴って亜鉛塩または亜鉛酸塩と反応して酸化
亜鉛を生成するので均一な粒子径のものが得られるもの
と考えられる。
In the present invention, the reaction is carried out in the presence of an organic compound that generates a base or acid through hydrolysis without directly adding a base or acid, so as the base or acid is generated in the aqueous solution, zinc salt or It is thought that since zinc oxide is produced by reacting with zincate, particles with a uniform particle size can be obtained.

以下、本発明を実施例に基づいて更に詳細に説明する。Hereinafter, the present invention will be explained in more detail based on examples.

実施例 1水2800モルに塩酸0.5モル、塩化亜鉛
1モル、へキサメチレンテトラミン2モルを溶解した混
合水溶液を約100ooで6■功ロ熱するとさらさらし
た白色沈澱を生じた。
Example 1 A mixed aqueous solution prepared by dissolving 0.5 mol of hydrochloric acid, 1 mol of zinc chloride, and 2 mol of hexamethylenetetramine in 2,800 mol of water was heated at about 100 oo for 6 hours to produce a free-flowing white precipitate.

これを櫨過、洗浄、乾燥した。電子顕微鏡写真によれば
図面に示すように粒度の均一な針状酸化亜鉛粒子である
ことが判る。粒度は約4仏mで粒度分布は3〜5〃m、
収率は対理論値で80%であった。実施例 2 水2800モルに硝酸0.5モル、硝酸亜鉛5モル、へ
キサメチレンテトラミン5モルを溶解した混合水溶液を
約100午0で60分加熱したところ均一な粒度の針状
酸化亜鉛粒子を得た。
This was filtered, washed and dried. The electron micrograph shows that the particles are acicular zinc oxide particles with uniform particle size, as shown in the drawing. The particle size is about 4 meters, and the particle size distribution is 3 to 5 meters.
The yield was 80% of theory. Example 2 A mixed aqueous solution of 0.5 mol of nitric acid, 5 mol of zinc nitrate, and 5 mol of hexamethylenetetramine dissolved in 2,800 mol of water was heated at about 100 am for 60 minutes to form acicular zinc oxide particles of uniform particle size. Obtained.

粒度は約3仏mで粒度分布は1〜5Am、収率は対理論
値で80%であった。実施例 3 水2800モルに水酸化ナトリウム50モル、酢酸亜鉛
5モル、エチレンクロルヒドリン5モルを溶解した混合
水溶液を約100ooで60分加熱したところ均一な粒
度の針状酸化亜鉛粒子を得た。
The particle size was about 3 mm, the particle size distribution was 1 to 5 Am, and the yield was 80% of theory. Example 3 A mixed aqueous solution prepared by dissolving 50 moles of sodium hydroxide, 5 moles of zinc acetate, and 5 moles of ethylene chlorohydrin in 2800 moles of water was heated at about 100 oo for 60 minutes to obtain acicular zinc oxide particles of uniform particle size. .

粒度は約8〃m、粒度分布は8〜12仏m、収率は対理
論値で90%であった。実施例 4水2800モルに水
酸化ナトリウム25モル、塩化亜鉛25モル、エチレン
クロルヒドリン15モルを溶解した混合水溶液を約10
0ooで60分加熱したところ均一な粒度の針状酸化亜
鉛粒子を得た。
The particle size was about 8 m, the particle size distribution was 8 to 12 m, and the yield was 90% of the theoretical value. Example 4 A mixed aqueous solution of 25 moles of sodium hydroxide, 25 moles of zinc chloride, and 15 moles of ethylene chlorohydrin dissolved in 2800 moles of water is
When heated for 60 minutes at 0oo, acicular zinc oxide particles with uniform particle size were obtained.

粒度は約1ムm、粒度分布は1〜2ムm、収率は対理論
値で90%であった。実施例 5 水2800モルに水酸化ナトリウム25モル、硝酸亜鉛
25モル、エチレンクロルヒドリン15モルを溶解した
混合水溶液を約1000○で60分加熱したところ均一
な粒度の針状酸化亜鉛粒子を得た。
The particle size was about 1 mm, the particle size distribution was 1-2 mm, and the yield was 90% of theory. Example 5 A mixed aqueous solution prepared by dissolving 25 moles of sodium hydroxide, 25 moles of zinc nitrate, and 15 moles of ethylene chlorohydrin in 2800 moles of water was heated at about 1000° for 60 minutes to obtain acicular zinc oxide particles of uniform particle size. Ta.

粒度は約2ムm、粒度分布は1〜5仏m、収率は対理論
値で90%であった。実施例 6 水2800モルに水酸化ナトリウム50モル、酢酸亜鉛
5モル、酢酸エチル5モルを溶解した混合水溶液を約1
00ooで60分加熱したところ均一な粒度の針状酸化
亜鉛粒子を得た。
The particle size was about 2 mm, the particle size distribution was 1 to 5 mm, and the yield was 90% of theory. Example 6 A mixed aqueous solution of 50 moles of sodium hydroxide, 5 moles of zinc acetate, and 5 moles of ethyl acetate dissolved in 2800 moles of water is
When heated at 00oo for 60 minutes, acicular zinc oxide particles of uniform particle size were obtained.

粒度は約9rm、粒度分布は8〜12仏m、収率は対理
論値で90%であった。実施例 7 水2800モルに水酸化ナトリウム25モル、塩化亜鉛
25モル、酢酸エチル15モルを溶解した混合水溶液を
約100q0で60分加熱したところ均一な粒度の針状
酸化亜鉛粒子を得た。
The particle size was about 9 rm, the particle size distribution was 8 to 12 m, and the yield was 90% of theory. Example 7 A mixed aqueous solution prepared by dissolving 25 moles of sodium hydroxide, 25 moles of zinc chloride, and 15 moles of ethyl acetate in 2800 moles of water was heated at about 100 q0 for 60 minutes to obtain acicular zinc oxide particles of uniform particle size.

粒度は約1山m、粒度分布は1〜2仏m、収率は対理論
値で90%であつた。実施例 8 水2800モルに水酸化ナトリウム25モル、硝酸亜鉛
25モル、酢酸エチル15モルを溶解した混合水溶液を
約100ooで6び分間加熱したところ均一な粒度の針
状酸化亜鉛粒子を得た。
The particle size was about 1 m, the particle size distribution was 1 to 2 m, and the yield was 90% of theory. Example 8 A mixed aqueous solution prepared by dissolving 25 moles of sodium hydroxide, 25 moles of zinc nitrate, and 15 moles of ethyl acetate in 2800 moles of water was heated at about 100 oo for 6 minutes to obtain acicular zinc oxide particles of uniform particle size.

粒度は2仏m、粒度分布は1〜54m、収率は対理論値
で90%であった。アルカリを用いて得られた酸化亜鉛
粒子の電子顕微鏡写真を第2図に示す。
The particle size was 2 meters, the particle size distribution was 1 to 54 meters, and the yield was 90% of theory. FIG. 2 shows an electron micrograph of zinc oxide particles obtained using an alkali.

これは実施例8の場合のものである。以上詳細に述べて
きたことから明らかなように、本発明では従来の亜鉛蒸
気の酸化による生成法のように高温装置やキャリアガス
を使用することなく、均一な粒子径を有する針状酸化亜
鉛粒子を得ることができ、更に従来例のように球状や板
状等の不整形のものを含まないため、触媒として利用し
た場合極めて有用な触媒となり、触媒反応産業に貢献す
るところ大である。
This is the case in Example 8. As is clear from what has been described in detail above, the present invention produces acicular zinc oxide particles having a uniform particle size without using a high-temperature device or a carrier gas unlike the conventional production method by oxidizing zinc vapor. Furthermore, since it does not contain irregular shapes such as spherical or plate-like shapes as in conventional examples, it is an extremely useful catalyst when used as a catalyst, and will greatly contribute to the catalytic reaction industry.

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

第1、2図は実施例1、8により得られた針状酸化亜鉛
粒子の電子顕微鏡写真図である。 第1図 第2図
1 and 2 are electron micrographs of acicular zinc oxide particles obtained in Examples 1 and 8. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1 酸を添加した塩化亜鉛,硝酸亜鉛,硫酸亜鉛,酢酸
亜鉛水溶液の少なくとも一種類を出発原料とし、これに
、有機化合物であるヘキサメチレンテトラミンを添加し
、または塩化亜鉛,硝酸亜鉛,硫酸亜鉛,酢酸亜鉛の少
なくとも一種類を出発原料とし前記出発原料の水溶液に
アルカリを添加し得られた亜鉛酸水溶液に、有機化合物
であるエチレンクロルヒドリン,酢酸エチルのいずれか
一種類を添加し、針状酸化亜鉛粒子を得ることを特徴と
する針状酸化亜鉛粒子の生成法。
1. At least one of zinc chloride, zinc nitrate, zinc sulfate, and zinc acetate aqueous solution to which an acid has been added is used as a starting material, and to this, an organic compound hexamethylenetetramine is added, or zinc chloride, zinc nitrate, zinc sulfate, At least one type of zinc acetate is used as a starting material, and an alkali is added to the aqueous solution of the starting material. To the resulting zinc acid aqueous solution, one type of organic compound, ethylene chlorohydrin or ethyl acetate, is added to form a needle-shaped A method for producing acicular zinc oxide particles, characterized by obtaining zinc oxide particles.
JP9122681A 1981-06-12 1981-06-12 Method for producing acicular zinc oxide particles Expired JPS6029645B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9122681A JPS6029645B2 (en) 1981-06-12 1981-06-12 Method for producing acicular zinc oxide particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9122681A JPS6029645B2 (en) 1981-06-12 1981-06-12 Method for producing acicular zinc oxide particles

Publications (2)

Publication Number Publication Date
JPS57205320A JPS57205320A (en) 1982-12-16
JPS6029645B2 true JPS6029645B2 (en) 1985-07-11

Family

ID=14020502

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9122681A Expired JPS6029645B2 (en) 1981-06-12 1981-06-12 Method for producing acicular zinc oxide particles

Country Status (1)

Country Link
JP (1) JPS6029645B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002274847A (en) * 2001-03-16 2002-09-25 National Institute For Materials Science Manufacturing method of acicular zinc oxide

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2683389B2 (en) * 1987-11-16 1997-11-26 花王株式会社 Flaky zinc oxide powder and method for producing the same
US5132104A (en) * 1989-07-21 1992-07-21 Lion Corporation Needle shaped monoamine complex of zinc carbonate and process for producing it
ZA965687B (en) * 1995-07-13 1997-02-24 Henkel Corp Inhibited pickling acids containing chloride and zinc ions.
ES2170675B1 (en) * 2000-06-27 2003-12-16 Consejo Superior Investigacion PROCEDURE FOR OBTAINING ZNO PARTICLES WITH ACICULAR MORPHOLOGY.
JP2008094696A (en) * 2006-10-16 2008-04-24 Sakai Chem Ind Co Ltd Fine needle zinc oxide
JP4853221B2 (en) * 2006-10-16 2012-01-11 堺化学工業株式会社 Method for producing acicular zinc oxide

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002274847A (en) * 2001-03-16 2002-09-25 National Institute For Materials Science Manufacturing method of acicular zinc oxide
JP4737577B2 (en) * 2001-03-16 2011-08-03 独立行政法人物質・材料研究機構 Manufacturing method of acicular zinc oxide

Also Published As

Publication number Publication date
JPS57205320A (en) 1982-12-16

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