JPH0687609A - Silicon dioxide fine powder for resin filler - Google Patents

Silicon dioxide fine powder for resin filler

Info

Publication number
JPH0687609A
JPH0687609A JP16035892A JP16035892A JPH0687609A JP H0687609 A JPH0687609 A JP H0687609A JP 16035892 A JP16035892 A JP 16035892A JP 16035892 A JP16035892 A JP 16035892A JP H0687609 A JPH0687609 A JP H0687609A
Authority
JP
Japan
Prior art keywords
silicon dioxide
fine powder
powder
resin
dioxide powder
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
JP16035892A
Other languages
Japanese (ja)
Other versions
JP3291588B2 (en
Inventor
Seiichi Honda
誠一 本多
Hiroshi Ikeda
洋 池田
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.)
Nippon Aerosil Co Ltd
Original Assignee
Nippon Aerosil 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=15713252&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JPH0687609(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Nippon Aerosil Co Ltd filed Critical Nippon Aerosil Co Ltd
Priority to JP16035892A priority Critical patent/JP3291588B2/en
Publication of JPH0687609A publication Critical patent/JPH0687609A/en
Application granted granted Critical
Publication of JP3291588B2 publication Critical patent/JP3291588B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Oxygen, Ozone, And Oxides In General (AREA)
  • Silicon Compounds (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To prevent a silicon dioxide fine powder from becoming cloudy at the time of mixing with a resin and to obtain a low torque value by giving hydrophobic treatment to silicon dioxide fine powder obtained by flame hydrolysis of halogenated silane by an organic silicon compound before mechanically crushing. CONSTITUTION:Gaseous silicon tetrachloride is passed through the flame of oxygen and hydrogen and given hydrolysis under high temperatures to obtain fine powder is silicon dioxide. An organic silicon compound for hydrophobic treatment is that which is combined with hydroxide groups of the surface of the silicon dioxide fine powder to block them and in itself has hydrophobic groups. For example, it is hexamethyldisilazane. Its used quantity is 0.5-40wt.% of the raw material, silicon dioxide fine powder. Reaction conditions of the hydrophobic treatment are not specially limited, but both the compounds are mixed in an atmosphere of inert gas and kept at 60-350 deg.C for 10min to 4hr before the mixture is dried to remove unreacted substances and by-products. After hydrophobic treatment, the product is pulverized by a ball mill, etc., to obtain powder of 80-180m<2>/g specific surface area, 80-300g/l bulk density and <=10kg.cm torque reference after resin filling.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、各種樹脂組成物に添加
した際に、樹脂の透明性を損なわず、かつ硬化前のトル
ク値を低く維持できる疎水化された二酸化珪素微粉末の
製造方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a hydrophobized silicon dioxide fine powder which, when added to various resin compositions, does not impair the transparency of the resin and can maintain a low torque value before curing. Regarding

【0002】室温硬化型エラストマー、接着剤、あるい
は高温加硫型シリコンゴム等として用いられる各種樹脂
組成物において、硬化後に高い強度特性を賦与するため
に樹脂に充填剤を添加する場合が多く、従来、二酸化珪
素粉末が充填剤として用いられている。一方、これらの
樹脂組成物は、成形時間や成形時の取扱い易さなどの点
から、硬化前のトルク値ができるだけ低く、具体的には
10Kg・cm以下であることが求められる。ところが、一
般に充填剤の添加量が多くなると樹脂のトルク値が高く
なり、通常の二酸化珪素粉末用いた場合には、これを4
0重量部程度を添加して必要強度を達成する条件下で、
10Kg・cm以下のトルク値を得るのは難しい。
In various resin compositions used as room temperature curable elastomers, adhesives, high temperature vulcanizing silicone rubbers, etc., fillers are often added to the resin in order to impart high strength properties after curing, and it is conventional. , Silicon dioxide powder is used as a filler. On the other hand, these resin compositions are required to have a torque value before curing as low as possible, specifically 10 kg / cm or less, from the viewpoints of molding time, handling ease during molding, and the like. However, in general, the larger the amount of filler added, the higher the torque value of the resin.
Under the condition that about 0 parts by weight is added to achieve the required strength,
It is difficult to obtain a torque value of 10 kg / cm or less.

【0003】そこで、従来、二酸化珪素粉末を比表面積
80m2 /g〜180m2 /g、嵩比重80g/l 〜300g/
l に微細化し、かつ疎水化することにより低トルク値を
得る試みがなされているが、従来の上記二酸化珪素粉末
には凝集物が多く含まれるため、これを樹脂に充填する
と樹脂の透明性を損なう問題がある。一例として、シリ
コンオイル100重量部に従来の二酸化珪素粉末微粉末
40重量部を添加したときのトルク値は8Kg・cmである
が、凝集物が多く含まれているために樹脂が白濁し透明
性が損なわれる。この凝集物は、二酸化珪素の微粒子が
凝集して生じる粒径約1mm程度の白色の粗粒子であり、
樹脂に添加して機械的に撹拌混合しても分散しない。
[0003] Therefore, conventionally, a specific surface area of the silicon dioxide powder 80m 2 / g~180m 2 / g, bulk density 80 g / l to 300 g /
Attempts have been made to obtain a low torque value by making it finer to l and making it hydrophobic, but since the above-mentioned conventional silicon dioxide powder contains many agglomerates, filling this with a resin will make the resin transparent. There is a damaging problem. As an example, the torque value when adding 40 parts by weight of the conventional fine powder of silicon dioxide powder to 100 parts by weight of silicone oil is 8 kg · cm, but the resin is clouded and transparent because it contains a lot of aggregates. Is damaged. The agglomerates are white coarse particles having a particle size of about 1 mm, which are generated by agglomeration of silicon dioxide fine particles,
It does not disperse even if it is added to the resin and mechanically mixed by stirring.

【0004】[0004]

【発明の解決課題】本発明は、従来の上記課題を解決す
るものであって、樹脂に添加された際に、樹脂の透明性
を損なわず、しかも低トルク値を与える疎水化された二
酸化珪素微粉末の製造方法を提供することを目的とす
る。
DISCLOSURE OF THE INVENTION The present invention is to solve the above-mentioned problems of the prior art, and when added to a resin, does not impair the transparency of the resin, and further imparts a low torque value to the hydrophobized silicon dioxide. An object is to provide a method for producing fine powder.

【0005】従来、比表面積80m2 /g〜180m2 /
g、嵩比重80g/l 〜300g/l の疎水化された二酸化
珪素微粉末は、ハロゲン化シランの火炎加水分解によっ
て得た二酸化珪素を有機珪素化合物の疎水化剤と共に機
械的に粉砕し、あるいは該二酸化珪素を機械的に粉砕し
た後に疎水化処理して製造されている。本発明者らは、
従来の二酸化珪素粉末に含有される凝集物は、該粉末を
機械的に粉砕して微粒子化する際に生じ、流動性の悪い
粉体に過度の機械的粉砕力が加わることが原因であるこ
とを見出し、二酸化珪素粉末を疎水化処理した後に粉砕
すれば凝集物の少ない二酸化珪素の微粒子を得ることが
できる知見を得た。
Conventionally, the specific surface area is 80 m 2 / g to 180 m 2 /
g, hydrophobized silicon dioxide fine powder having a bulk specific gravity of 80 g / l to 300 g / l is obtained by mechanically grinding silicon dioxide obtained by flame hydrolysis of halogenated silane together with a hydrophobizing agent of an organosilicon compound, or It is manufactured by mechanically grinding the silicon dioxide and then hydrophobizing it. We have
Aggregates contained in conventional silicon dioxide powder are generated when the powder is mechanically pulverized into fine particles, and are caused by excessive mechanical pulverization force applied to the powder having poor fluidity. The present inventors have found that it is possible to obtain fine particles of silicon dioxide with less agglomerates by pulverizing the silicon dioxide powder after hydrophobizing it.

【0006】[0006]

【課題の解決手段:発明の構成】本発明によれば、ハロ
ゲン化シランの火炎加水分解によって得た二酸化珪素微
粉末を有機珪素化合物によって疎水化処理した後に機械
的に粉砕することを特徴とする二酸化珪素微粉末の製造
方法が提供される。
According to the present invention, a silicon dioxide fine powder obtained by flame hydrolysis of a halogenated silane is hydrophobized with an organic silicon compound and then mechanically pulverized. A method for producing silicon dioxide fine powder is provided.

【0007】本発明に用いられるハロゲン化シランの火
炎加水分解によって生じた二酸化珪素粉末とは、例えば
特公昭47−46274号の製法によって製造された二
酸化珪素粉末を云う。この製法は、四塩化珪素ガスを酸
素と水素の火炎中に通じ、高温下で加水分解させる方法
であり、二酸化珪素の微粒子が得られる。
The silicon dioxide powder produced by flame hydrolysis of the halogenated silane used in the present invention means, for example, the silicon dioxide powder produced by the method disclosed in Japanese Patent Publication No. 47-46274. This production method is a method in which silicon tetrachloride gas is passed through a flame of oxygen and hydrogen to cause hydrolysis at high temperature, and fine particles of silicon dioxide are obtained.

【0008】上記二酸化珪素の疎水化処理は、従来行な
われているこの種の疎水化処理方法によって行なうこと
ができ、使用する有機珪素化合物も一般に疎水化剤とし
て用いるものであれば良い。一般に用いられている疎水
化剤は二酸化珪素粉末表面の水酸基何等かの形で結合し
てこれを封鎖し、かつ自身が疎水基を有する化合物であ
って、実用されているのは、疎水基を有するシランカッ
プリング剤、シリル化剤などであり、具体的には、例え
ば、ヘキサメチルジシラザン、ヘキサメチルジシロキサ
ン、トリメチルシラノール、トリメチルシランエトキシ
ド、トリメチルシランメトキシドなどのオルガノシロキ
サンやオルガノポリシロキサンなどが好適に用いられ
る。
The hydrophobizing treatment of silicon dioxide can be carried out by a conventional hydrophobizing method of this kind, and the organosilicon compound to be used may be one generally used as a hydrophobizing agent. A commonly used hydrophobizing agent is a compound that binds in some form and blocks the hydroxyl group on the surface of silicon dioxide powder, and has a hydrophobic group by itself. A silane coupling agent, a silylating agent, or the like, and specifically, for example, an organosiloxane such as hexamethyldisilazane, hexamethyldisiloxane, trimethylsilanol, trimethylsilaneethoxide, trimethylsilanemethoxide, or an organopolysiloxane. Are preferably used.

【0009】疎水化剤として使用される上記有機珪素化
合物の使用量は特に限定されないが、実用上、原料の二
酸化珪素微粉末に対して0.5〜40重量%が好まし
い。使用量が0.5重量%より少ないと、疎水化の効果
が低く、また使用量が40重量%を越えても疎水化の効
果は大きな差はない。また、疎水化処理の反応条件も特
に限定されないが、好適には、不活性ガス雰囲気下で6
0℃〜350℃の温度範囲で上記有機珪素化合物を二酸
化珪素粉末に混合し10分〜4時間保持した後に乾燥
し、未反応物および副生成物を除去する方法によれば良
い。不活性ガス雰囲気下で疎水化反応を行なわせること
により疎水化剤の酸化が防止される。反応温度が60℃
よりも低いと十分に疎水化反応が進行せず、また350
℃よりも高いと疎水化剤が熱分解するので好ましくな
い。
The amount of the above-mentioned organosilicon compound used as a hydrophobizing agent is not particularly limited, but in practice, it is preferably 0.5 to 40% by weight based on the raw material silicon dioxide fine powder. When the amount used is less than 0.5% by weight, the effect of hydrophobizing is low, and even when the amount used exceeds 40% by weight, there is no great difference in the effect of hydrophobicizing. Further, the reaction conditions for the hydrophobizing treatment are not particularly limited, but preferably 6 under an inert gas atmosphere.
A method may be used in which the organosilicon compound is mixed with the silicon dioxide powder in a temperature range of 0 ° C. to 350 ° C., and the mixture is held for 10 minutes to 4 hours and then dried to remove unreacted substances and by-products. Oxidation of the hydrophobizing agent is prevented by carrying out the hydrophobizing reaction in an inert gas atmosphere. Reaction temperature is 60 ℃
If it is lower than this, the hydrophobic reaction does not proceed sufficiently,
If the temperature is higher than ° C, the hydrophobizing agent is thermally decomposed, which is not preferable.

【0010】原料の二酸化珪素粉末を疎水化処理した後
に、比表面積80m2 /g〜180m2 /g、嵩比重80g/
l 〜300g/l になるまで機械的に粉砕する。機械的粉
砕手段は、ボールミル、コニカルミル、タワーミルなど
通常の粉砕機を用いることができる。また、石臼などの
ように磨砕力を利用して粉砕しても良い。粉砕条件も特
に限定されない。一例として、通常のボールミルを用い
て粉砕する場合には、10〜200rpm の回転数で、5
分〜8時間撹拌すれば良い。なお、比表面積および嵩比
重が上記範囲外であるときは、この二酸化珪素粉末を樹
脂に添加した場合、樹脂の硬化前のトルク値が10Kg・
cm以上になる。
[0010] The silicon dioxide powder of the raw material after the hydrophobic treatment, a specific surface area of 80m 2 / g~180m 2 / g, bulk density 80 g /
Grind mechanically until l-300 g / l. As the mechanical crushing means, a usual crusher such as a ball mill, a conical mill or a tower mill can be used. Further, it may be crushed by utilizing the grinding force like a stone mill. Grinding conditions are also not particularly limited. As an example, when pulverizing with a normal ball mill, the number of revolutions should be 5 to 5 at a rotation speed of 10 to 200 rpm.
It suffices to stir for minutes to 8 hours. When the specific surface area and bulk specific gravity are out of the above ranges, when the silicon dioxide powder is added to the resin, the torque value before curing the resin is 10 kg.
More than cm.

【0011】原料の二酸化珪素粉末を疎水化処理した後
に粉砕することにより、凝集物が少ない二酸化珪素の微
粉末が得られる。なお、機械的粉砕処理を疎水化処理と
同時に行なう場合には、機械的粉砕後に疎水化処理する
方法よりも、樹脂に添加した場合に樹脂の白濁の程度は
少ないが透明性を維持する点でまだ不十分である。これ
は疎水化処理が十分に行なわれない段階で二酸化珪素粉
末が機械的に粉砕されるために依然として凝集物が発生
し、透明性に影響を与える程度の量の凝集物が含まれる
ためであると考えられる。
By finely grinding the raw material silicon dioxide powder after hydrophobizing it, fine powder of silicon dioxide containing few agglomerates can be obtained. When the mechanical pulverization treatment is carried out simultaneously with the hydrophobizing treatment, the degree of cloudiness of the resin when added to the resin is less than that of the method of performing the hydrophobizing treatment after the mechanical pulverization, but in that the transparency is maintained. Still not enough. This is because the silicon dioxide powder is mechanically pulverized at a stage where the hydrophobization treatment is not sufficiently performed, so that the agglomerates are still generated, and the agglomerates are contained in an amount that affects the transparency. it is conceivable that.

【0012】[0012]

【発明の効果】本発明の製造方法によって得られた二酸
化珪素微粉末は樹脂に混入したときに白濁を生じること
がなく、かつ低いトルク値を得ることができる。一例と
して、シリコーンオイル100重量部に該二酸化珪素微
粉末を40重量部混合すると、トルク値8Kg・cmの透明
な樹脂組成物が得られる。
The silicon dioxide fine powder obtained by the production method of the present invention does not cause clouding when mixed with resin, and a low torque value can be obtained. As an example, by mixing 40 parts by weight of the silicon dioxide fine powder with 100 parts by weight of silicone oil, a transparent resin composition having a torque value of 8 kg · cm can be obtained.

【0013】[0013]

【実施例および比較例】以下、本発明を実施例に基づい
て具体的に説明するが、以下の実施例は本発明を限定す
るものではない。
EXAMPLES AND COMPARATIVE EXAMPLES The present invention will be specifically described below based on examples, but the following examples do not limit the present invention.

【0014】実施例1 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil200)200
g にヘキサメチルジシラザン13g を加えて混合した後
に、150℃で熱処理を行ない211gの疎水化された
二酸化珪素粉末を得た。この二酸化珪素粉末を内容積4
00リットルのボールミルに装入し、2時間粉砕して比
表面積160m2 /g、嵩比重240g/l の微粉末を得
た。この二酸化珪素粉末40部と透明なシリコーンオイ
ル(商品名KF96:10000CS)100部をロータミキサーに
入れて混合(60rpm,30℃,15 分間)し、ラボプラストミ
ル(東洋精機社製)を用い、シリコーンオイルのトルク
値を測定した。トルク値は8Kg・cmであった。また上記
二酸化珪素粉末を混合したシリコーンオイルは白濁せず
透明であった。
Example 1 Silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (manufactured by Nippon Aerosil Co., Ltd .: trade name Aerosil 200) 200
After 13 g of hexamethyldisilazane was added to and mixed with g, heat treatment was carried out at 150 ° C. to obtain 211 g of hydrophobized silicon dioxide powder. This silicon dioxide powder has an internal volume of 4
It was charged into a 00 liter ball mill and pulverized for 2 hours to obtain a fine powder having a specific surface area of 160 m 2 / g and a bulk specific gravity of 240 g / l. 40 parts of this silicon dioxide powder and 100 parts of transparent silicone oil (trade name KF96: 10000CS) were put in a rotor mixer and mixed (60 rpm, 30 ° C, 15 minutes), and a Labo Plastomill (manufactured by Toyo Seiki Co., Ltd.) was used. The torque value of the silicone oil was measured. The torque value was 8 kg · cm. The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0015】実施例2 実施例1の二酸化粉末に代えて、疎水化処理された他の
二酸化珪素粉末(日本アエロジル社製:商品名RY200 )
を用い、実施例1と同様に粉砕処理して比表面積105
2 /g、嵩比重148g/l の二酸化珪素粉末を得た。こ
の粉体を実施例1と同一の条件でシリコーンオイルに添
加してトルク値を測定したところ、5Kg・cmであった。
また上記二酸化珪素粉末を混合したシリコーンオイルは
白濁せず透明であった。
Example 2 Instead of the dioxide powder of Example 1, another hydrophobized silicon dioxide powder (manufactured by Nippon Aerosil Co., Ltd .: trade name RY200)
Was pulverized in the same manner as in Example 1 to obtain a specific surface area of 105
A silicon dioxide powder having a m 2 / g and a bulk specific gravity of 148 g / l was obtained. This powder was added to silicone oil under the same conditions as in Example 1 and the torque value was measured and found to be 5 kg · cm.
The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0016】実施例3 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil200)200
g にトリメチルエトキシシラン4Kgを加えて混合した後
に、150℃で熱処理を行ない疎水化された二酸化珪素
粉末を得た。この二酸化珪素粉末を内容積400リット
ルのボールミルに装入し、2時間粉砕して比表面積15
1m2 /g、嵩比重86g/l の微粉末を得た。この二酸化
珪素粉末を実施例1と同一の条件でシリコーンオイルに
添加してトルク値を測定したところ、9Kg・cmであっ
た。また上記二酸化珪素粉末を混合したシリコーンオイ
ルは白濁せず透明であった。
Example 3 Silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (manufactured by Nippon Aerosil Co., Ltd .: trade name Aerosil 200) 200
After adding and mixing 4 kg of trimethylethoxysilane to g, heat treatment was performed at 150 ° C. to obtain a hydrophobized silicon dioxide powder. This silicon dioxide powder was charged into a ball mill having an internal volume of 400 liters and pulverized for 2 hours to give a specific surface area of 15
A fine powder having a volume specific gravity of 1 m 2 / g and a bulk specific gravity of 86 g / l was obtained. The silicon dioxide powder was added to silicone oil under the same conditions as in Example 1 and the torque value was measured and found to be 9 kg · cm. The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0017】比較例1 実施例3の処理工程において、疎水化処理に先立って原
料の二酸化珪素粉末を粉砕して嵩比重135g/l にした
後に、180℃の温度下で疎水化処理を行なう以外は実
施例3と同様に処理して、比表面積140m2 /g、嵩比
重150g/l の二酸化珪素粉末を得た。この粉体を実施
例1と同一の条件でシリコーンオイルに添加してトルク
値を測定したところ、トルク値は9Kg・cmであったが、
シリコーンオイルは白濁していた。
Comparative Example 1 In the treatment step of Example 3, except that the raw material silicon dioxide powder was pulverized to a bulk specific gravity of 135 g / l prior to the hydrophobic treatment, and then the hydrophobic treatment was carried out at a temperature of 180 ° C. Was treated in the same manner as in Example 3 to obtain a silicon dioxide powder having a specific surface area of 140 m 2 / g and a bulk specific gravity of 150 g / l. When this powder was added to silicone oil under the same conditions as in Example 1 and the torque value was measured, the torque value was 9 kg · cm.
The silicone oil was cloudy.

【0018】比較例2 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil200)20Kg
とトリメチルエトキシシラン4Kgを内容積400リット
ルのボールミルに入れ、70℃に保って、60rpm で2
時間回転した後に、内容物を窒素気流中にて200℃、
2時間保持し、未反応物および副生物を揮発除去した。
得られた疎水化された二酸化珪素粉末の比表面積は15
8m2 /g、嵩比重214g/l であった。この粉体を実施
例1と同一の条件でシリコーンオイルに添加してトルク
値を測定したところ、トルク値は8Kg・cmであったが、
シリコーンオイルは白濁していた。
Comparative Example 2 20 kg of silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (product name Aerosil200, manufactured by Nippon Aerosil Co., Ltd.)
And 4 kg of trimethylethoxysilane were placed in a ball mill with an internal volume of 400 liters, kept at 70 ° C, and then 2 at 60 rpm.
After rotating for an hour, the contents were heated to 200 ° C in a nitrogen stream,
It was kept for 2 hours to volatilize and remove unreacted materials and by-products.
The specific surface area of the obtained hydrophobized silicon dioxide powder is 15
The specific gravity was 8 m 2 / g and the bulk specific gravity was 214 g / l. When this powder was added to silicone oil under the same conditions as in Example 1 and the torque value was measured, the torque value was 8 kg · cm.
The silicone oil was cloudy.

【手続補正書】[Procedure amendment]

【提出日】平成5年8月26日[Submission date] August 26, 1993

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】全文[Correction target item name] Full text

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【書類名】 明細書[Document name] Statement

【発明の名称】 樹脂充填材用二酸化珪素微粉末[Title of Invention] Silicon dioxide fine powder for resin filler

【特許請求の範囲】[Claims]

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、各種樹脂組成物に添加
した際に、樹脂の透明性を損なわず、かつ硬化前のトル
ク値を低く維持できる樹脂充填用二酸化珪素微粉末に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a resin-filled silicon dioxide fine powder which, when added to various resin compositions, can maintain a low torque value before curing without impairing the transparency of the resin.

【0002】室温硬化型エラストマー、接着剤、あるい
は高温加硫型シリコンゴム等として用いられる各種樹脂
組成物において、硬化後に高い強度特性を賦与するため
に樹脂に充填材を添加する場合が多く、従来、二酸化珪
素粉末が充填材として用いられている。一方、これらの
樹脂組成物は、成形時間や成形時の取扱い易さなどの点
から、硬化前のトルク値ができるだけ低く、具体的には
10Kg・cm以下であることが求められる。ところ
が、一般に充填材の添加量が多くなると樹脂のトルク値
が高くなり、通常の二酸化珪素粉末用いた場合には、こ
れを40重量部程度を添加して必要強度を達成する条件
下で、10Kg・cm以下のトルク値を得るのは難し
い。
In various resin compositions used as room temperature curable elastomers, adhesives, high temperature vulcanizing silicone rubbers, etc., fillers are often added to the resin in order to impart high strength characteristics after curing, , Silicon dioxide powder is used as a filler. On the other hand, these resin compositions are required to have a torque value before curing as low as possible, specifically, 10 Kg · cm or less, from the viewpoints of molding time and handling during molding. However, generally, when the amount of the filler added is increased, the torque value of the resin is increased, and when the usual silicon dioxide powder is used, it is added under the condition that about 40 parts by weight of this is added to achieve the required strength. -It is difficult to obtain a torque value of cm or less.

【0003】そこで、従来、二酸化珪素粉末を比表面積
80m/g〜180m/g、嵩比重80〜300g
/lに疎水化し、かつ圧密することにより低トルク値を
得る試みがなされているが、従来の上記二酸化珪素粉末
には凝集物が多く含まれるため、これを樹脂に充填する
と樹脂の透明性を損なう問題がある。一例として、シリ
コンオイル100重量部に従来の二酸化珪素粉末微粉末
40重量部を添加したときのトルク値は8Kg・cmで
あるが、凝集物が多く含まれているために樹脂が白濁し
透明性が損なわれる。この凝集物は、二酸化珪素の微粒
子が凝集して生じる粒径約1mm程度の白色の粗粒子で
あり、樹脂に添加して機械的に撹拌混合しても分散しな
い。
[0003] Therefore, conventionally, a specific surface area of the silicon dioxide powder 80m 2 / g~180m 2 / g, bulk density 80~300g
Attempts have been made to obtain a low torque value by hydrophobizing to 1 / l and consolidating. However, since the above-mentioned conventional silicon dioxide powder contains a lot of agglomerates, filling this with a resin will make the resin transparent. There is a damaging problem. As an example, the torque value when adding 40 parts by weight of the conventional fine powder of silicon dioxide powder to 100 parts by weight of silicone oil is 8 kg · cm, but the resin is clouded and transparent because it contains a lot of aggregates. Is damaged. The agglomerates are white coarse particles having a particle diameter of about 1 mm generated by agglomeration of fine particles of silicon dioxide, and do not disperse even if they are added to a resin and mechanically stirred and mixed.

【0004】[0004]

【発明の解決課題】本発明は、従来の上記課題を解決す
るものであって、樹脂に添加された際に、樹脂の透明性
を損なわず、しかも低トルク値を与える疎水化された樹
脂充填用二酸化珪素微粉末を提供することを目的とす
る。
DISCLOSURE OF THE INVENTION The present invention is to solve the above-mentioned problems of the prior art, and when added to a resin, it does not impair the transparency of the resin, and yet it has a low torque value and is filled with a hydrophobic resin. The object is to provide a silicon dioxide fine powder for use.

【0005】従来、比表面積80〜180m/g、嵩
比重80〜300g/lの疎水化された二酸化珪素微粉
末は、ハロゲン化シランの火炎加水分解によって得た二
酸化珪素を有機珪素化合物の疎水化剤と共に機械的に粉
砕し、あるいは該二酸化珪素を機械的に粉砕した後に疎
水化処理して製造されている。本発明者らは、従来の二
酸化珪素粉末に含有される凝集物は、該粉末を機械的に
粉砕して微粒子化する際に生じ、流動性の悪い粉体に過
度の機械的粉砕力が加わることが原因であることを見出
し、二酸化珪素粉末を疎水化処理した後に粉砕すれば凝
集物の少ない二酸化珪素の微粒子を得ることができ、こ
れは樹脂に充填した場合に、樹脂の透明性を損なわず、
しかも低トルク値を与えることができる知見を得た。本
発明はかかる知見に基づいて従来の上記問題を解決し
た。
Conventionally, a hydrophobized silicon dioxide fine powder having a specific surface area of 80 to 180 m 2 / g and a bulk specific gravity of 80 to 300 g / l is obtained by subjecting silicon dioxide obtained by flame hydrolysis of a halogenated silane to a hydrophobized organosilicon compound. It is manufactured by mechanically grinding with an agent or by mechanically grinding the silicon dioxide and then hydrophobizing it. The present inventors have found that the agglomerates contained in the conventional silicon dioxide powder are generated when the powder is mechanically pulverized into fine particles, and excessive mechanical pulverization force is applied to the powder having poor fluidity. It was found that this was caused by the fact that the silicon dioxide powder was subjected to a hydrophobizing treatment and then pulverized to obtain fine particles of silicon dioxide with few agglomerates. This impairs the transparency of the resin when it is filled in the resin. No
Moreover, we have obtained the knowledge that a low torque value can be given. The present invention has solved the above-mentioned conventional problems based on such findings.

【0006】[0006]

【発明の構成】本発明によれば以下の樹脂充填用二酸化
珪素微粉末が提供される。 (1) 樹脂充填材用二酸化珪素微粉末であって、樹脂
に充填後の基準トルク値が10Kg・cm以下であり、
樹脂の透明性を維持する二酸化珪素微粉末。 (2) 比表面積80〜180m/g、嵩比重80〜
300g/lであって、樹脂に充填後の基準トルク値が
10Kg・cm以下であり、樹脂の透明性を維持する上
記(1)の二酸化珪素微粉末。
According to the present invention, the following silicon dioxide fine powder for resin filling is provided. (1) A silicon dioxide fine powder for a resin filler, which has a reference torque value of 10 Kg · cm or less after filling the resin,
Silicon dioxide fine powder that maintains the transparency of the resin. (2) Specific surface area 80 to 180 m 2 / g, bulk specific gravity 80 to
The silicon dioxide fine powder of (1) above, which has a reference torque value of 10 kg / cm or less after filling the resin with 300 g / l and maintains the transparency of the resin.

【0007】[0007]

【発明の具体的な説明】本発明に用いられる二酸化珪素
粉末はハロゲン化シランの火炎加水分解によって得られ
るものであり、例えば、特公昭47−46274号の製
法によって製造される。この製法は、四塩化珪素ガスを
酸素と水素の火炎中に通じ、高温下で加水分解させる方
法であり、二酸化珪素の微粒子が得られる。
DETAILED DESCRIPTION OF THE INVENTION The silicon dioxide powder used in the present invention is obtained by flame hydrolysis of a halogenated silane, and is produced, for example, by the method disclosed in JP-B-47-46274. This production method is a method in which silicon tetrachloride gas is passed through a flame of oxygen and hydrogen to cause hydrolysis at high temperature, and fine particles of silicon dioxide are obtained.

【0008】本発明の二酸化珪素粉末は有機珪素化合物
によって疎水化処理されたものである。疎水化処理の方
法は従来行なわれている方法によって行なうことがで
き、使用する有機珪素化合物も一般に疎水化剤として用
いるものであれば良い。一般に用いられている疎水化剤
は二酸化珪素粉末表面の水酸基何等かの形で結合してこ
れを封鎖し、かつ自身が疎水基を有する化合物であっ
て、実用されているのは、疎水基を有するシランカップ
リング剤、シリル化剤などであり、具体的には、例え
ば、ヘキサメチルジシラザン、ヘキサメチルジシロキサ
ン、トリメチルシラノール、トリメチルシランエトキシ
ド、トリメチルシランメトキシドなどのオルガノシロキ
サンやオルガノポリシロキサンなどが好適に用いられ
る。
The silicon dioxide powder of the present invention is hydrophobized with an organic silicon compound. The method of hydrophobizing treatment can be carried out by a conventionally used method, and the organosilicon compound used may be one generally used as a hydrophobizing agent. A commonly used hydrophobizing agent is a compound that binds in some form and blocks the hydroxyl group on the surface of silicon dioxide powder, and has a hydrophobic group by itself. A silane coupling agent, a silylating agent, or the like, and specifically, for example, an organosiloxane such as hexamethyldisilazane, hexamethyldisiloxane, trimethylsilanol, trimethylsilaneethoxide, trimethylsilanemethoxide, or an organopolysiloxane. Are preferably used.

【0009】疎水化剤として使用される上記有機珪素化
合物の使用量は特に限定されないが、実用上、原料の二
酸化珪素微粉末に対して0.5〜40重量%が好まし
い。使用量が0.5重量%より少ないと、疎水化の効果
が低く、また使用量が40重量%を越えても疎水化の効
果は大きな差はない。また、疎水化処理の反応条件も特
に限定されないが、好適には、不活性ガス雰囲気下で6
0℃〜350℃の温度範囲で上記有機珪素化合物を二酸
化珪素粉末に混合し10分〜4時間保持した後に乾燥
し、未反応物および副生成物を除去する方法によれば良
い。不活性ガス雰囲気下で疎水化反応を行なわせること
により疎水化剤の酸化が防止される。反応湿度が60℃
よりも低いと十分に疎水化反応が進行せず、また350
℃よりも高いと疎水化剤が熱分解するので好ましくな
い。
The amount of the above-mentioned organosilicon compound used as a hydrophobizing agent is not particularly limited, but in practice, it is preferably 0.5 to 40% by weight based on the raw material silicon dioxide fine powder. When the amount used is less than 0.5% by weight, the effect of hydrophobizing is low, and even when the amount used exceeds 40% by weight, there is no great difference in the effect of hydrophobicizing. Further, the reaction conditions for the hydrophobizing treatment are not particularly limited, but preferably 6 under an inert gas atmosphere.
A method may be used in which the organosilicon compound is mixed with the silicon dioxide powder in a temperature range of 0 ° C. to 350 ° C., and the mixture is held for 10 minutes to 4 hours and then dried to remove unreacted substances and by-products. Oxidation of the hydrophobizing agent is prevented by carrying out the hydrophobizing reaction in an inert gas atmosphere. Reaction humidity is 60 ° C
If it is lower than this, the hydrophobic reaction does not proceed sufficiently,
If the temperature is higher than ° C, the hydrophobizing agent is thermally decomposed, which is not preferable.

【0010】原料の二酸化珪素粉末を疎水化処理した後
に、比表面積80〜180m/g、嵩比重80〜30
0g/lになるまで機械的に粉砕する。機械的粉砕手段
は、ボールミル、コニカルミル、タワーミルなど通常の
粉砕機を用いることができる。また、石臼などのように
磨砕力を利用して粉砕しても良い。粉砕条件も特に限定
されない。一例として、通常のボールミルを用いて粉砕
する場合には、10〜200rpmの回転数で、5分〜
8時間撹拌すれば良い。なお、比表面積および嵩比重が
上記範囲外であるときは、この二酸化珪素粉末を樹脂に
添加した場合、樹脂の硬化前のトルク値が10Kg・c
m以上になる。
After hydrophobizing the raw material silicon dioxide powder, it has a specific surface area of 80 to 180 m 2 / g and a bulk specific gravity of 80 to 30.
Grind mechanically to 0 g / l. As the mechanical crushing means, a usual crusher such as a ball mill, a conical mill or a tower mill can be used. Further, it may be crushed by utilizing the grinding force like a stone mill. Grinding conditions are also not particularly limited. As an example, in the case of crushing using a normal ball mill, the number of rotations is 10 to 200 rpm and 5 minutes to
Stir for 8 hours. When the specific surface area and the bulk specific gravity are out of the above ranges, when the silicon dioxide powder is added to the resin, the torque value before curing the resin is 10 Kg · c.
m or more.

【0011】原料の二酸化珪素粉末を疎水化処理した後
に機械的に粉砕することにより、凝集物が少ない二酸化
珪素の微粉末が得られる。なお、機械的粉砕処理を疎水
化処理と同時に行なう場合には、機械的粉砕後に疎水化
処理する方法よりも、樹脂に添加した場合に樹脂の白濁
の程度は少ないが透明性を維持する点でまだ不十分であ
る。これは疎水化処理が十分に行なわれない段階で二酸
化珪素粉末が機械的に粉砕されるために依然として凝集
物が発生し、透明性に影響を与える程度の量の凝集物が
含まれるためであると考えられる。
By finely grinding silicon dioxide powder as a raw material and then mechanically pulverizing it, a fine powder of silicon dioxide containing few agglomerates can be obtained. When the mechanical pulverization treatment is carried out simultaneously with the hydrophobizing treatment, the degree of cloudiness of the resin when added to the resin is less than that of the method of performing the hydrophobizing treatment after the mechanical pulverization, but in that the transparency is maintained. Still not enough. This is because the silicon dioxide powder is mechanically pulverized at a stage where the hydrophobization treatment is not sufficiently performed, so that the agglomerates are still generated, and the agglomerates are contained in an amount that affects the transparency. it is conceivable that.

【0012】[0012]

【発明の効果】以上のようにして得られる本発明の二酸
化珪素微粉末は樹脂に混入したときに白濁を生じること
がなく、かつ低いトルク値を得ることができる。一例と
して、シリコーンオイル100重量部に該二酸化珪素微
粉末を40重量部混合すると、トルク値8Kg・cmの
透明な樹脂組成物が得られる。なお、本明細書におい
て、説明の便宜上、シリコーンオイル100重量部に二
酸化珪素微粉末を40重量部混合したときのトルク値を
基準トルク値とする。
Industrial Applicability The silicon dioxide fine powder of the present invention obtained as described above does not cause clouding when mixed with a resin, and a low torque value can be obtained. As an example, by mixing 40 parts by weight of the silicon dioxide fine powder with 100 parts by weight of silicone oil, a transparent resin composition having a torque value of 8 kg · cm can be obtained. In this specification, for convenience of description, a torque value when 40 parts by weight of silicon dioxide fine powder is mixed with 100 parts by weight of silicone oil is used as a reference torque value.

【0013】[0013]

【実施例および比較例】以下、本発明を実施例に基づい
て具体的に説明するが、以下の実施例は本発明を限定す
るものではない。
EXAMPLES AND COMPARATIVE EXAMPLES The present invention will be specifically described below based on examples, but the following examples do not limit the present invention.

【0014】実施例1 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil20
0)200gにヘキサメチルジシラザン13gを加えて
混合した後に、150℃で熱処理を行ない211gの疎
水化された二酸化珪素粉末を得た。この二酸化珪素粉末
を内容積4リットルのボールミルに装入し、2時間粉砕
して比表面積160m/g、嵩比重240g/lの微
粉末を得た。この二酸化珪素粉末40部と透明なシリコ
ーンオイル(商品名KF96:10000CS)100
部をロータミキサーに入れて混合(60rpm,30
℃,15分間)し、ラボプラストミル(東洋精機社製)
を用い、シリコーンオイルの基準トルク値を測定したと
ころ、8Kg・cmであった。また上記二酸化珪素粉末
を混合したシリコーンオイルは白濁せず透明であった。
Example 1 Silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (product name Aerosil 20 manufactured by Nippon Aerosil Co., Ltd.)
0) 13 g of hexamethyldisilazane was added to 200 g and mixed, and then heat treated at 150 ° C. to obtain 211 g of hydrophobized silicon dioxide powder. This silicon dioxide powder was charged into a ball mill having an internal volume of 4 liters and pulverized for 2 hours to obtain a fine powder having a specific surface area of 160 m 2 / g and a bulk specific gravity of 240 g / l. 40 parts of this silicon dioxide powder and 100 of transparent silicone oil (trade name KF96: 10000CS)
Part into a rotor mixer and mix (60 rpm, 30
℃, 15 minutes), Labo Plastomill (Toyo Seiki Co., Ltd.)
When the standard torque value of the silicone oil was measured using, it was 8 Kg · cm. The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0015】実施例2 実施例1の二酸化粉末に代えて、疎水化処理された他の
二酸化珪素粉末(日本アエロジル社製:商品名RY20
0)を用い、実施例1と同様に粉砕処理して比表面積1
05m/g、嵩比重148g/lの二酸化珪素粉末を
得た。この粉体を実施例1と同一の条件でシリコーンオ
イルに添加して基準トルク値を測定したところ、5Kg
・cmであった。また上記二酸化珪素粉末を混合したシ
リコーンオイルは白濁せず透明であった。
Example 2 Instead of the dioxide powder of Example 1, another hydrophobized silicon dioxide powder (manufactured by Nippon Aerosil Co., Ltd .: trade name RY20) is used.
0) and pulverized in the same manner as in Example 1 to give a specific surface area of 1
05m 2 / g, to obtain a silicon dioxide powder of bulk density 148 g / l. This powder was added to silicone oil under the same conditions as in Example 1 to measure the reference torque value.
・ It was cm. The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0016】実施例3 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil20
0)200gにトリメチルエトキシシラン40gを加え
て混合した後に、150℃で熱処理を行ない疎水化され
た二酸化珪素粉末を得た。この二酸化珪素粉末を内容積
4リットルのボールミルに装入し、2時間粉砕して比表
面積151m/g、嵩比重86g/lの微粉末を得
た。この二酸化珪素粉末を実施例1と同一の条件でシリ
コーンオイルに添加して基準トルク値を測定したとこ
ろ、9Kg・cmであった。また上記二酸化珪素粉末を
混合したシリコーンオイルは白濁せず透明であった。
Example 3 Silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (product name Aerosil 20 manufactured by Nippon Aerosil Co., Ltd.)
0) 40 g of trimethylethoxysilane was added to 200 g and mixed, and then heat treated at 150 ° C. to obtain a hydrophobized silicon dioxide powder. This silicon dioxide powder was charged into a ball mill having an internal volume of 4 liters and pulverized for 2 hours to obtain a fine powder having a specific surface area of 151 m 2 / g and a bulk specific gravity of 86 g / l. When this silicon dioxide powder was added to silicone oil under the same conditions as in Example 1 and the reference torque value was measured, it was 9 Kg · cm. The silicone oil mixed with the silicon dioxide powder was transparent without clouding.

【0017】比較例1 実施例3の処理工程において、疎水化処理に先立って原
料の二酸化珪素粉末を粉砕して嵩比重135g/lにし
た後に、180℃の温度下で疎水化処理を行なう以外は
実施例3と同様に処理して、比表面積140m/g、
嵩比重150g/lの二酸化珪素粉末を得た。この粉体
を実施例1と同一の条件でシリコーンオイルに添加して
基準トルク値を測定したところ、9Kg・cmであった
が、シリコーンオイルは白濁していた。
Comparative Example 1 In the treatment step of Example 3, the raw material silicon dioxide powder was pulverized to a bulk specific gravity of 135 g / l prior to the hydrophobic treatment, and then the hydrophobic treatment was carried out at a temperature of 180 ° C. Was treated in the same manner as in Example 3 to give a specific surface area of 140 m 2 / g,
A silicon dioxide powder having a bulk specific gravity of 150 g / l was obtained. When this powder was added to silicone oil under the same conditions as in Example 1 and the reference torque value was measured, it was 9 Kg · cm, but the silicone oil was cloudy.

【0018】比較例2 四塩化珪素を酸水素炎中で加水分解して得た二酸化珪素
粉末(日本アエロジル社製:商品名Aerosil20
0)20Kgとトリメチルエトキシシラン4Kgを内容
積400リットルのボールミルに入れ、70℃に保っ
て、60rpmで2時間回転した後に、内容物を窒素気
流中にて200℃、2時間保持し、未反応物および副生
物を揮発除去した。得られた疎水化された二酸化珪素粉
末の比表面積は158m/g、嵩比重214g/lで
あった。この粉体を実施例1と同一の条件でシリコーン
オイルに添加して基準トルク値を測定したところ、8K
g・cmであったが、シリコーンオイルは白濁してい
た。
Comparative Example 2 Silicon dioxide powder obtained by hydrolyzing silicon tetrachloride in an oxyhydrogen flame (product name Aerosil 20 manufactured by Nippon Aerosil Co., Ltd.)
0) 20 kg and 4 kg of trimethylethoxysilane were placed in a ball mill having an internal volume of 400 liters, kept at 70 ° C. and rotated at 60 rpm for 2 hours, and then the contents were kept at 200 ° C. for 2 hours in a nitrogen stream to react unreacted. The substances and by-products were removed by volatilization. The hydrophobized silicon dioxide powder obtained had a specific surface area of 158 m 2 / g and a bulk specific gravity of 214 g / l. This powder was added to silicone oil under the same conditions as in Example 1 to measure the reference torque value.
It was g · cm, but the silicone oil was cloudy.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ハロゲン化シランの火炎加水分解によっ
て得た二酸化珪素微粉末を有機珪素化合物によって疎水
化処理した後に機械的に粉砕することを特徴とする二酸
化珪素微粉末の製造方法。
1. A method for producing fine silicon dioxide powder, which comprises subjecting fine silicon dioxide powder obtained by flame hydrolysis of halogenated silane to hydrophobic treatment with an organosilicon compound and then mechanically pulverizing the fine powder.
【請求項2】 ハロゲン化シランの火炎加水分解によっ
て得た二酸化珪素微粉末を有機珪素化合物によって疎水
化処理した後に、比表面積80m2 /g〜180m2 /g、
嵩比重80g/l 〜300g/l に機械的に粉砕する請求項
1の方法。
Wherein the silicon dioxide fine powder obtained by flame hydrolysis of halogenated silane after hydrophobic treatment with an organic silicon compound, a specific surface area of 80m 2 / g~180m 2 / g,
The method according to claim 1, wherein the bulk specific gravity is mechanically crushed to 80 g / l to 300 g / l.
JP16035892A 1992-05-27 1992-05-27 Silicon dioxide fine powder for resin filler Expired - Fee Related JP3291588B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16035892A JP3291588B2 (en) 1992-05-27 1992-05-27 Silicon dioxide fine powder for resin filler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16035892A JP3291588B2 (en) 1992-05-27 1992-05-27 Silicon dioxide fine powder for resin filler

Publications (2)

Publication Number Publication Date
JPH0687609A true JPH0687609A (en) 1994-03-29
JP3291588B2 JP3291588B2 (en) 2002-06-10

Family

ID=15713252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16035892A Expired - Fee Related JP3291588B2 (en) 1992-05-27 1992-05-27 Silicon dioxide fine powder for resin filler

Country Status (1)

Country Link
JP (1) JP3291588B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004099075A1 (en) 2003-05-06 2004-11-18 Tokuyama Corporation Hydrophobic fumed silica
US7282236B2 (en) 1999-12-22 2007-10-16 Degussa Gmbh Hydrophobic silica
JP2009520667A (en) * 2005-12-23 2009-05-28 エボニック デグサ ゲーエムベーハー Silanized fumed silica
JP2010528132A (en) * 2007-05-22 2010-08-19 エボニック デグサ ゲーエムベーハー Silane-treated and ground fumed silica
JP2011506657A (en) * 2007-12-11 2011-03-03 エボニック デグサ ゲーエムベーハー Coating system
CN102530962A (en) * 2010-12-10 2012-07-04 中国科学院过程工程研究所 Method for synthesizing hydrophobic nanometer silicon dioxide particle through combustion method
WO2022091953A1 (en) 2020-10-30 2022-05-05 株式会社トクヤマ Method for producing rubber composition, fumed silica for rubber composition, and rubber composition

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7282236B2 (en) 1999-12-22 2007-10-16 Degussa Gmbh Hydrophobic silica
WO2004099075A1 (en) 2003-05-06 2004-11-18 Tokuyama Corporation Hydrophobic fumed silica
US7507389B2 (en) 2003-05-06 2009-03-24 Tokuyama Corporation Hydrophobic fumed silica
JP2009520667A (en) * 2005-12-23 2009-05-28 エボニック デグサ ゲーエムベーハー Silanized fumed silica
US8211971B2 (en) 2005-12-23 2012-07-03 Evonik Degussa Gmbh Fumed silanized silica
US8552107B2 (en) 2005-12-23 2013-10-08 Evonik Degussa Gmbh Fumed silanized silica
JP2010528132A (en) * 2007-05-22 2010-08-19 エボニック デグサ ゲーエムベーハー Silane-treated and ground fumed silica
JP2011506657A (en) * 2007-12-11 2011-03-03 エボニック デグサ ゲーエムベーハー Coating system
CN102530962A (en) * 2010-12-10 2012-07-04 中国科学院过程工程研究所 Method for synthesizing hydrophobic nanometer silicon dioxide particle through combustion method
CN102530962B (en) * 2010-12-10 2015-06-03 中国科学院过程工程研究所 Method for synthesizing hydrophobic nanometer silicon dioxide particle through combustion method
WO2022091953A1 (en) 2020-10-30 2022-05-05 株式会社トクヤマ Method for producing rubber composition, fumed silica for rubber composition, and rubber composition
KR20230098174A (en) 2020-10-30 2023-07-03 가부시키가이샤 도쿠야마 Manufacturing method of rubber composition, fumed silica for rubber composition and rubber composition

Also Published As

Publication number Publication date
JP3291588B2 (en) 2002-06-10

Similar Documents

Publication Publication Date Title
JP5130227B2 (en) Silicon dioxide produced by densified pyrolysis for crust formation
US4615741A (en) Filler for electronic element encapsulation resin and electronic element encapsulation resin composition containing the same
KR102566641B1 (en) Granulation treated silica and preparing method thereof
JP6192730B2 (en) Method for producing an insulating mixture
JP2003171118A (en) Hydrophobic silica fine powder and method for producing the same
WO2019167618A1 (en) Fused spherical silica powder and manufacturing method therefor
KR20160037945A (en) Method for producing crushed silica particles, and resin composition containing said particles
JPH0687609A (en) Silicon dioxide fine powder for resin filler
JP4968569B2 (en) Highly dispersible hydrophobic silica fine powder and production method thereof
JP2000256008A (en) Hydrophobic fumed silica and method for producing the same
US4780108A (en) Method for increasing bulk density of fillers
JP5637691B2 (en) polymer
JP3445707B2 (en) Siliceous filler and its production method
JP2000191317A (en) Method for producing fused spherical silica
JP3374156B2 (en) Surface modified silicon dioxide fine powder
CA1263204A (en) Method for increasing the bulk density of fillers
EP4043398A1 (en) Silica with reduced tribo-charge for toner applications
JPS59204633A (en) Resin composition with low radioactivity
JPH02158637A (en) Silica filler and sealing resin composition using the same
CN119242074B (en) A hydrophobic fumed nano-silica and its preparation method and application
JPS60108465A (en) Filler densified with polymer
JPH02145415A (en) Fused spherical silica and sealing resin composition using the same as filler
JPH11323096A (en) Resin composition for sealing use
JPH11293125A (en) Resin composition for sealing use

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees