JPS61251509A - Production of spherical silica powder - Google Patents

Production of spherical silica powder

Info

Publication number
JPS61251509A
JPS61251509A JP9233485A JP9233485A JPS61251509A JP S61251509 A JPS61251509 A JP S61251509A JP 9233485 A JP9233485 A JP 9233485A JP 9233485 A JP9233485 A JP 9233485A JP S61251509 A JPS61251509 A JP S61251509A
Authority
JP
Japan
Prior art keywords
silica powder
powder
silica
particle size
slurry
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP9233485A
Other languages
Japanese (ja)
Other versions
JPH0336762B2 (en
Inventor
Motohiko Yoshizumi
素彦 吉住
Susumu Miyama
晋 深山
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.)
Mitsubishi Metal Corp
Original Assignee
Mitsubishi Metal 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 Mitsubishi Metal Corp filed Critical Mitsubishi Metal Corp
Priority to JP9233485A priority Critical patent/JPS61251509A/en
Publication of JPS61251509A publication Critical patent/JPS61251509A/en
Publication of JPH0336762B2 publication Critical patent/JPH0336762B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:A slurry of silica powder in water or an organic solvent is spray-dried and roasted to give spherical silica particles which are added to rubber or resins to increase abrasion resistance and friction without any adverse effect on toughness. CONSTITUTION:Silica powder is dispersed in water or an organic solvent, and spray-dried. The powder is roasted at 800-1,200 deg.C. The silica powder to be roasted has preferably more than 30m<2>/g of specific surface area. The organic solvent used is, e.g., an alcohol or ketone boiling at an appropriate temperature. The concentration of the slurry is about 5-30wt% as a silica powder.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、耐摩耗性と共に摩擦性を高めるためにゴム、
樹脂などに添加され、しかも靭性にも悪影響を与えない
添加物として好適な球状シリカ粉末の製造方法に関する
[Detailed Description of the Invention] <Industrial Application Field> The present invention uses rubber,
The present invention relates to a method for producing spherical silica powder that is suitable as an additive that is added to resins and the like and does not adversely affect toughness.

〈従来技術と問題点〉 用されている。一般にこのような添加物としては比表面
積30 tr?/I以上の微細粉が使用されている。
<Prior art and problems> Used. Generally, such additives have a specific surface area of 30 tr? /I or more fine powder is used.

ところが耐摩耗性の他に高摩耗性即ち摩擦力が大きい性
質を賦与する場合はむしろ比較的粒度が粗く、平均粒径
1.θ〜100μのシリカ粉末が用いられる。次にシリ
カの形状としては球形が好ましい。
However, when imparting properties such as high abrasion properties, that is, large frictional force in addition to wear resistance, the particle size is rather coarse, and the average particle size is 1. Silica powder of θ to 100μ is used. Next, the shape of the silica is preferably spherical.

これは球形のほうが樹脂に含有されやすく、含有量を多
くできるからである。特にエポキシ樹脂に含有させてL
SIの封止剤として用いる場合にはシリカの含有量が大
きくしかもシリカの純度が高いことが必要である。更に
シリカ粉末には空孔が無いことも求められる。空孔が存
在すると空孔中のガスが樹脂等に悪影響を与えるおそれ
がある。
This is because spherical particles are more easily contained in the resin, and the content can be increased. In particular, L is added to epoxy resin.
When used as a sealant for SI, it is necessary that the silica content is large and the purity of the silica is high. Furthermore, the silica powder is also required to be free of pores. If pores exist, the gas in the pores may have an adverse effect on the resin and the like.

シリカ粉末を得るには一般に天然の珪石を粉砕する方法
と2人工的にシリカ粉末を合成する方法とがある。とこ
ろが天然の珪石を粉砕してシリカ粉末を得る方法は粒度
を揃えることが難しく、また形状も不規則であl)、S
iOの純度も低い。一方1人工的にシリカ粉末を合成す
る方法には(1)ケイ酸塩と酸の中和反応によって生ず
る沈澱を用いる方法、 (n)四塩化ケイ素と水蒸気と
を気相で反応させる方法2等がある。ところがこのよう
な合成方法によって得られるシリカ粉末は高純度の粉末
が得られるものの比表面積は30m//i以Δ9.靭性
や摩擦性を高める為に添加されるものとしては粒度が微
細に過ぎる。
Generally, there are two ways to obtain silica powder: one is to crush natural silica stone, and the other is to artificially synthesize silica powder. However, in the method of obtaining silica powder by crushing natural silica stone, it is difficult to make the particle size uniform, and the shape is irregular.
The purity of iO is also low. On the other hand, methods for artificially synthesizing silica powder include (1) a method using a precipitate produced by the neutralization reaction of a silicate and an acid, (n) a method of reacting silicon tetrachloride with water vapor in the gas phase, etc. There is. However, although the silica powder obtained by such a synthesis method is a highly pure powder, the specific surface area is Δ9. The particle size is too fine to be added to improve toughness and friction.

このため従来は上記合成方法によって得られた微細なシ
リカ粉末を1000℃以上の高温で焼成したものや。
For this reason, conventionally, fine silica powder obtained by the above synthesis method was fired at a high temperature of 1000° C. or higher.

一旦溶融したシリカ塊等を必要とする粒度まで粉砕して
所定のシリカ粉末を得ている。しかしこの方法によって
得られるシリカ粉末は粉砕して粒度を揃えるため形状が
不規則であシ、かつ粒度分布も広い。このためとのシリ
カ粉末をゴム、樹脂に添加すると靭性に著しい悪影響を
及ぼすという問題がある。
A predetermined silica powder is obtained by crushing a molten silica lump or the like to a required particle size. However, since the silica powder obtained by this method is pulverized to make the particle size uniform, its shape is irregular and the particle size distribution is wide. If silica powder is added to rubber or resin for this purpose, there is a problem in that it has a significant adverse effect on toughness.

〈発明の構成〉 本発明は、微細なシリカ粉末を溶媒に分散させて噴霧乾
燥することによシシリカ粉末を個々に適度な粒度に凝集
させ、これを所定温度にて焼成し好適な粒度の球状シリ
カとすることによシ上記従来技術の問題を解消している
。即ち1本発明によれば。
<Structure of the Invention> In the present invention, fine silica powder is dispersed in a solvent and spray-dried to agglomerate individual silica powders to a suitable particle size, and then baked at a predetermined temperature to form spherical particles with a suitable particle size. By using silica, the problems of the prior art described above are solved. That is, according to one invention.

シリカ粉末を水または有機溶媒に分散させた後。After dispersing the silica powder in water or organic solvent.

このスラリーを噴霧乾燥し、SOO〜1200℃の温度
範囲で焼成することを特徴とする球状シリカの製造方法
が提供される。
A method for producing spherical silica is provided, which comprises spray-drying this slurry and firing it at a temperature ranging from SOO to 1200°C.

本発明においては、まずシリカ粉末を水または有機溶媒
に分散する。この分散媒としては、水の他、アルコール
類、ケトン類等の有機溶媒のうち適夏な沸点を有するも
のを使用できる。またこれらの分散媒に低温で分解、揮
発するような可溶性の樹脂を少量添加してもよい。この
樹脂は結合剤として役立ち焼成時間を短くする効果があ
る。分散手段は特に制限されない。例えば攪拌している
分散媒中にシリカ粉末をそのまま徐々に添加してもよい
In the present invention, silica powder is first dispersed in water or an organic solvent. As this dispersion medium, in addition to water, organic solvents such as alcohols and ketones having a suitable boiling point can be used. Further, a small amount of soluble resin that decomposes and evaporates at low temperatures may be added to these dispersion media. This resin serves as a binder and has the effect of shortening the firing time. The dispersion means is not particularly limited. For example, the silica powder may be gradually added as it is to the dispersion medium being stirred.

尚、ボールミル、サンドグライダ−等を用いれば短時間
で高濃度のスラリーを得ることができる。
Note that a highly concentrated slurry can be obtained in a short time by using a ball mill, sand glider, or the like.

原料として用いるシリカ粉末は比表面積30〃9以上が
好ましい。この粒度より粗いと分散媒に分散し難くなる
The silica powder used as a raw material preferably has a specific surface area of 30.9 or more. If the particle size is coarser than this, it becomes difficult to disperse in the dispersion medium.

スラリーの濃度は特に限定されないが分散媒に対してシ
リカ粉末を5〜30重量%とすると良い。
Although the concentration of the slurry is not particularly limited, it is preferable that the silica powder be 5 to 30% by weight based on the dispersion medium.

スラリーの濃度は造粒粉ひいては焼成後の粉末粒度に影
響するので、得ようとする粉末の粒径によって定めれば
良い。尚、濃度が高過ぎると粘度が高くなりすぎ噴霧で
きない。一方、濃度が低すぎると多量のスラリーを用い
る必要があり製造効率が悪くなる。
Since the concentration of the slurry affects the granulated powder and ultimately the powder particle size after firing, it may be determined depending on the particle size of the powder to be obtained. Note that if the concentration is too high, the viscosity will become too high and spraying will not be possible. On the other hand, if the concentration is too low, it is necessary to use a large amount of slurry, resulting in poor production efficiency.

次に、このスラリーを噴霧乾燥する。用いる噴霧乾燥機
は、二流体ノズルを用いる型式、遠心噴霧の型式などい
ずれのものでも構わない。上記スラリーは噴霧されるこ
とにより適度な大きさの粒子に凝集して造粒される。
This slurry is then spray dried. The spray dryer used may be of any type, such as a two-fluid nozzle type or a centrifugal spray type. The above slurry is agglomerated into particles of appropriate size and granulated by being sprayed.

噴霧乾燥された粉末はサイクロン等で捕集し。The spray-dried powder is collected using a cyclone or the like.

その後焼成する。焼成温度はSOO〜1200℃である
。800℃より低いと造粒粒子内における焼結速度が小
さいため、如何に長時間焼成しても空孔の残在する粉末
しか得られない。一方焼成温度が1200℃を越えると
造粒粉どうしでの焼成が起こシ始めるので粉末が必要以
上に粗大化し、かつ粒度も不均一になる。焼成時間は原
料となるシリカ粉末の粒度や焼成温度によって異なるが
1通常3〜20時間程度焼成すれば空孔のない球状のシ
リカ粉末を得ることができる。
Then it is fired. The firing temperature is SOO to 1200°C. If the temperature is lower than 800° C., the sintering rate within the granulated particles is low, so no matter how long the firing is performed, only powder with residual pores is obtained. On the other hand, if the firing temperature exceeds 1200° C., the granulated powder starts to be fired together, resulting in the powder becoming coarser than necessary and the particle size becoming non-uniform. Although the firing time varies depending on the particle size of the raw silica powder and the firing temperature, it is usually possible to obtain spherical silica powder without voids by firing for about 3 to 20 hours.

〈発明の効果〉 本発明の方法で製造されるシリカ粉末は平均粒径が1.
0〜100μであシ、耐摩耗性と共に摩擦性を高めるた
めにゴム、樹脂などに添加される添加物として好適であ
る。さらに本発明で得られるシリカ粉末は球状でちゃ9
粒度も均一であるためゴム。
<Effects of the Invention> The silica powder produced by the method of the present invention has an average particle size of 1.
It has a thickness of 0 to 100μ and is suitable as an additive added to rubbers, resins, etc. to improve wear resistance and friction properties. Furthermore, the silica powder obtained by the present invention has a spherical shape.
Rubber because the particle size is uniform.

樹脂に添加しても靭性に悪影響を及ぼすことも無い。即
ち9本発明のシリカ粉末は粒子が均一な球形を有してい
るため樹脂等に分散させた場合に均一な分散状態となる
。従って不定形のシリカと比較すると同量を樹脂に添加
した場合、靭性の低下が少なく、従来の不定形シリカに
比べてより多量のシリカを添加できるので樹脂等の耐摩
耗性、高摩擦性をよシ一層向上できる。
Even when added to the resin, it does not have any adverse effect on the toughness. That is, since the particles of the silica powder of the present invention have a uniform spherical shape, when it is dispersed in a resin or the like, it becomes uniformly dispersed. Therefore, compared to irregularly shaped silica, when the same amount is added to resin, there is less decrease in toughness, and compared to conventional irregularly shaped silica, a larger amount of silica can be added, improving the wear resistance and high friction properties of resin etc. You can improve even further.

〈実施例〉 第1表に示すシリカ粉末50gを分散媒に分散させて所
定濃度のスラリーを調製した。次いでこのスラリーを直
径0.41111の孔を持つ二流体ノズルより約5cc
/分の速度で噴霧した。同時に噴霧乾線機での入口温度
が200℃の空気を0.5m/分の割合で流入し、噴霧
された凝集粒子の分散媒を蒸発させて、造粒粉を形成し
た。この造粒粉をサイクロンで回収し、その後表中に示
す雰囲気、温度および時間で焼成した。
<Example> 50 g of silica powder shown in Table 1 was dispersed in a dispersion medium to prepare a slurry of a predetermined concentration. Next, approximately 5 cc of this slurry was passed through a two-fluid nozzle with a diameter of 0.41111 mm.
It was sprayed at a speed of /min. At the same time, air having an inlet temperature of 200° C. was introduced into the spray drying line machine at a rate of 0.5 m/min to evaporate the dispersion medium of the sprayed aggregated particles to form granulated powder. This granulated powder was collected with a cyclone, and then fired under the atmosphere, temperature, and time shown in the table.

原料として使用したシリカ粉末の比表面積2分散媒の種
類5分散濃度、焼成時間および得られたシリカ粉末の性
状を第1表に纒めて示す。
Table 1 summarizes the specific surface area of the silica powder used as a raw material, the type of dispersion medium, the dispersion concentration, the firing time, and the properties of the obtained silica powder.

第1表から明らかなように本発明の方法によって得られ
たシリカ粉末はいずれも平均粒径が8〜46μ、比表面
積0.35〜0.09ぜ7gであシ、摩擦性を高めるた
めに好適な粒度を有していることが判る。更にとのシリ
カ粉末の形状はいずれも球形ないし略球形であシ1粒度
分布も均一に揃っており、ゴム、樹脂の靭性にも悪影響
のないものである。
As is clear from Table 1, all of the silica powders obtained by the method of the present invention have an average particle size of 8 to 46μ and a specific surface area of 0.35 to 0.09g. It can be seen that it has a suitable particle size. Furthermore, the shapes of the silica powders are all spherical or approximately spherical, and the particle size distribution is uniform, so that the toughness of rubber and resin is not adversely affected.

〈比較例〉 第2表に示す比表面積のシリカ粉末を用い、第2表に示
す所定の温度および時間で焼成した。得られたシリカ粉
末の性状を第2表に纒めて示す。
<Comparative Example> Silica powder having a specific surface area shown in Table 2 was used and fired at a predetermined temperature and time shown in Table 2. The properties of the obtained silica powder are summarized in Table 2.

第2表から明らかなように、原料のシリカ粉末が3.2
5 d/Iの比表面積のものは得られるシリカ粉末に多
数の空孔が存在する。また焼成温度が12509C,7
50℃のものも空孔が顕著にみとめられ、しかもその一
部は形状も不定である。
As is clear from Table 2, the raw material silica powder is 3.2
In the case of a silica powder having a specific surface area of 5 d/I, a large number of pores are present in the obtained silica powder. Also, the firing temperature is 12509C, 7
Even at 50° C., pores were clearly observed, and some of the pores were irregular in shape.

Claims (2)

【特許請求の範囲】[Claims] (1)シリカ粉末を水または有機溶媒に分散させた後、
このスラリーを噴霧乾燥し、800〜1200℃の温度
範囲で焼成することを特徴とする球状シリカ粉末の製造
方法。
(1) After dispersing silica powder in water or organic solvent,
A method for producing spherical silica powder, which comprises spray drying this slurry and firing at a temperature range of 800 to 1200°C.
(2)特許請求の範囲第1項の製造方法であつて、水ま
たは有機溶媒に分散するシリカ粉末の比表面積が30m
^2/g以上である方法。
(2) The manufacturing method according to claim 1, wherein the silica powder dispersed in water or an organic solvent has a specific surface area of 30 m
^2/g or more method.
JP9233485A 1985-05-01 1985-05-01 Production of spherical silica powder Granted JPS61251509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9233485A JPS61251509A (en) 1985-05-01 1985-05-01 Production of spherical silica powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9233485A JPS61251509A (en) 1985-05-01 1985-05-01 Production of spherical silica powder

Publications (2)

Publication Number Publication Date
JPS61251509A true JPS61251509A (en) 1986-11-08
JPH0336762B2 JPH0336762B2 (en) 1991-06-03

Family

ID=14051492

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9233485A Granted JPS61251509A (en) 1985-05-01 1985-05-01 Production of spherical silica powder

Country Status (1)

Country Link
JP (1) JPS61251509A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5028360A (en) * 1989-04-17 1991-07-02 Nitto Chemical Industries Co., Ltd. Method of manufacturing spherical silica particles

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5028360A (en) * 1989-04-17 1991-07-02 Nitto Chemical Industries Co., Ltd. Method of manufacturing spherical silica particles

Also Published As

Publication number Publication date
JPH0336762B2 (en) 1991-06-03

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