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JPH0336762B2 - - Google Patents
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JPH0336762B2 - - Google Patents

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Publication number
JPH0336762B2
JPH0336762B2 JP9233485A JP9233485A JPH0336762B2 JP H0336762 B2 JPH0336762 B2 JP H0336762B2 JP 9233485 A JP9233485 A JP 9233485A JP 9233485 A JP9233485 A JP 9233485A JP H0336762 B2 JPH0336762 B2 JP H0336762B2
Authority
JP
Japan
Prior art keywords
silica powder
silica
particle size
powder
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.)
Expired
Application number
JP9233485A
Other languages
Japanese (ja)
Other versions
JPS61251509A (en
Inventor
Motohiko Yoshizumi
Susumu Myama
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 Materials Corp
Original Assignee
Mitsubishi Materials 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 Materials Corp filed Critical Mitsubishi Materials 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

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  • Silicon Compounds (AREA)

Description

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

<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。 <従来技術と問題点> ゴム、樹脂などにシリカ粉末を添加すると耐摩
耗性が大幅に向上することが知られており、広く
利用されている。一般にこのような添加物として
は比表面積30m2/g以上の微細粉が使用されてい
る。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1.0〜100μ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。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LSI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。 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、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り、SiOの純度も低い。一
方、人工的にシリカ粉末を合成する方法には
()ケイ酸塩と酸の中和反応によつて生ずる沈
澱を用いる方法、()四塩化ケイ素と水蒸気と
を気相で反応させる方法、等がある。ところがこ
のような合成方法によつ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30m2
g以上であり、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。このため
従来は上記合成方法によつ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、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
法によつ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り、かつ粒度分布も
広い。このためこ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。 <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り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り上記従
来技術の問題を解消している。即ち、本発明によ
れば、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
カの製造方法が提供される。 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
適度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。例えば撹拌している
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。尚、ボールミル、サンドグライダー等を
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。 原料として用いるシリカ粉末は比表面積30m2
g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。 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。
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
つて定めれば良い。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。 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。 噴霧乾燥された粉末はサイクロン等で捕集し、
その後焼成する。焼成温度は800〜1200℃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存
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り始める
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
度や焼成温度によつて異なるが、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。 <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であり、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
カ粉末は球状であり、粒度も均一であるためゴ
ム、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、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。従つて不定形のシリカ
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対摩耗
性、高摩擦性をより一層向上できる。 <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0.4mmの孔を持つ二流体ノズルよ
り約5c.c./分の速度で噴霧した。同時に噴霧乾燥
機での入口温度が200℃の空気を0.5m3/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。 原料として使用したシリカ粉末の比表面積、分
散媒の種類、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。 第1表から明らかなように本発明の方法によつ
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0.35〜0.09m3/gであり、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。更にこのシリカ粉末の形状はいずれも球形な
いし略球形であり、粒度分布も均一に揃つてお
り、ゴム、樹脂の靭性にも悪影響のないものであ
る。 <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。 第2表から明らかなように、原料のシリカ粉末
が3.25m2/g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
1250℃、750℃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。
<Industrial Application Field> The present invention relates to a method for producing spherical silica powder, which is suitable as an additive that is added to rubbers, resins, etc. to improve wear resistance and friction properties, and does not adversely affect toughness. <Prior art and problems> It is known that adding silica powder to rubber, resin, etc. greatly improves wear resistance, and it is widely used. Generally, as such additives, fine powder having a specific surface area of 30 m 2 /g or more is used. However, when imparting properties such as high abrasion properties, that is, large frictional force in addition to wear resistance, silica powder having a relatively coarse particle size and an average particle size of 1.0 to 100 μm is used. Next, the shape of the silica is preferably spherical. This is because the spherical shape is easier to contain in the resin,
This is because the content can be increased. In particular, when it is incorporated into an epoxy resin and used as a sealant for LSI, 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. Generally, silica powder can be obtained by two methods: pulverizing natural silica stone and artificially synthesizing silica powder. However, in the method of obtaining silica powder by crushing natural silica stone, it is difficult to make the particle size uniform, the shape is irregular, and the purity of SiO is low. On the other hand, methods for artificially synthesizing silica powder include () a method using a precipitate produced by the neutralization reaction of a silicate and an acid, () 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 highly pure, the specific surface area is only 30 m 2 /
The particle size is too fine to be added to improve toughness and friction properties. For this reason, in the past, fine silica powder obtained by the above synthesis method was calcined at a high temperature of 1000°C or higher, or a predetermined silica powder was obtained by pulverizing a molten silica lump to the required particle size. ing. However, the silica powder obtained by this method has an irregular shape and a wide particle size distribution because it is pulverized to make the particle size uniform. Therefore, there is a problem in that when this silica powder is added to rubber or resin, it has a significant adverse effect on toughness. <Structure of the Invention> The present invention involves dispersing fine silica powder in a solvent and spray-drying it to agglomerate each silica powder to an appropriate particle size, and then firing this at a predetermined temperature to produce spherical silica particles with a suitable particle size. By doing so, the problems of the prior art described above are solved. That is, according to the present invention, after dispersing silica powder in water or an organic solvent, this slurry is spray-dried and heated at 800 to 1200°C.
Provided is a method for producing spherical silica characterized by firing at a temperature range of . In the present invention, silica powder is first dispersed in water or an organic solvent. As the dispersion medium, in addition to water, organic solvents having an appropriate boiling point such as alcohols and ketones 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. Note that if a ball mill, sand glider, etc. are used, a highly concentrated slurry can be obtained in a short time. The silica powder used as a raw material has a specific surface area of 30m 2 /
g or more is preferable. If the particle size is coarser than this, it becomes difficult to disperse in the dispersion medium. 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.
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. 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. The spray-dried powder is collected using a cyclone, etc.
Then it is fired. The firing temperature is 800-1200℃.
If the temperature is lower than 800°C, the sintering rate within the granulated particles will be low, so no matter how long the firing is performed, only powder with residual pores will be obtained. On the other hand, the firing temperature is 1200℃
If the temperature exceeds this value, calcination of the granulated powders will begin to occur, 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 silica powder used as the raw material and the firing temperature, it is usually possible to obtain spherical silica powder without voids by firing for about 3 to 20 hours. <Effects of the Invention> The silica powder produced by the method of the present invention has an average particle size of 1.0 to 100μ, and is suitable as an additive added to rubber, resin, etc. to improve wear resistance and friction properties. . Furthermore, since the silica powder obtained in the present invention is spherical and has a uniform particle size, it will not adversely affect the toughness even when added to rubber or resin. That is, since the particles of the silica powder of the present invention have a uniform spherical shape, when dispersed in a resin or the like, the particles become uniformly dispersed. Therefore, compared to irregularly shaped silica, when the same amount is added to resin, there is less decrease in toughness, and since a larger amount of silica can be added compared to conventional irregularly shaped silica, it improves the wear resistance and high friction properties of resin etc. can be further improved. <Example> 50 g of silica powder shown in Table 1 was dispersed in a dispersion medium to prepare a slurry of a predetermined concentration. This slurry was then sprayed at a rate of about 5 c.c./min through a two-fluid nozzle with a 0.4 mm diameter hole. At the same time, air having an inlet temperature of 200° C. was introduced into the spray dryer at a rate of 0.5 m 3 /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. 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 are summarized in Table 1. 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 8.
46μ and a specific surface area of 0.35 to 0.09 m 3 /g, which indicates that it has a particle size suitable for improving friction properties. Furthermore, the shape of this silica powder is spherical or approximately spherical, the particle size distribution is uniform, and the toughness of rubber and resin is not adversely affected. <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. As is clear from Table 2, when the raw material silica powder has a specific surface area of 3.25 m 2 /g, a large number of pores are present in the obtained silica powder. Also, the firing temperature
Voids were clearly observed in the samples heated to 1250℃ and 750℃.
Moreover, the shape of some of them is undefined.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 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。 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30m2/g以上である方法。
[Claims] 1. A method for producing spherical silica powder, which comprises dispersing silica powder in water or an organic solvent, spray-drying the slurry, and firing the slurry at a temperature in the range of 800 to 1200°C. 2. The manufacturing method set forth in claim 1, comprising:
A method in which the specific surface area of silica powder dispersed in water or an organic solvent is 30 m 2 /g or more.
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 JPS61251509A (en) 1986-11-08
JPH0336762B2 true 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)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2545282B2 (en) * 1989-04-17 1996-10-16 日東化学工業株式会社 Method for producing spherical silica particles

Also Published As

Publication number Publication date
JPS61251509A (en) 1986-11-08

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