JPH062569B2 - Silica fine powder - Google Patents

Silica fine powder

Info

Publication number
JPH062569B2
JPH062569B2 JP2416152A JP41615290A JPH062569B2 JP H062569 B2 JPH062569 B2 JP H062569B2 JP 2416152 A JP2416152 A JP 2416152A JP 41615290 A JP41615290 A JP 41615290A JP H062569 B2 JPH062569 B2 JP H062569B2
Authority
JP
Japan
Prior art keywords
silica
less
crushed
weight
fine
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 - Lifetime
Application number
JP2416152A
Other languages
Japanese (ja)
Other versions
JPH03247635A (en
Inventor
悌二郎 松本
隆祐 荒木
正道 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Seika Chemicals Co Ltd
Original Assignee
Sumitomo Seika Chemicals Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Seika Chemicals Co Ltd filed Critical Sumitomo Seika Chemicals Co Ltd
Priority to JP2416152A priority Critical patent/JPH062569B2/en
Publication of JPH03247635A publication Critical patent/JPH03247635A/en
Publication of JPH062569B2 publication Critical patent/JPH062569B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sealing Material Composition (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Epoxy Resins (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Structures Or Materials For Encapsulating Or Coating Semiconductor Devices Or Solid State Devices (AREA)
  • Silicon Compounds (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本発明は半導体等の電子部品封止用合成樹脂組成物等に
用いる微粉末に関する。更に詳しくは、該組成物の充填
剤等に適した角の丸まったシリカ微粉末粒子に関する。
The present invention relates to a fine powder used in a synthetic resin composition for sealing electronic parts such as semiconductors. More specifically, it relates to silica fine powder particles with rounded corners, which are suitable as a filler for the composition.

【0002】[0002]

【従来の技術・発明が解決しようとする課題】[Problems to be Solved by Conventional Techniques and Inventions]

半導体及び電子部品は、それを外部環境から保護するた
めにセラミックパッケージまたは樹脂などで封止されて
いるが、この封止材料についてはコスト、生産性等の面
から無機質充填剤を含有させた合成樹脂組成物によるも
のが普及している。 この合成樹脂組成物は、エポキシ樹脂などの熱硬化性樹
脂とシリカなどの無機質充填剤とから構成されている
が、これらの組成物は熱膨張係数が小さく、良熱伝導
性、低透湿性で機械的特性等にすぐれ、しかも低コスト
のものが望ましいことから、この無機湿充填剤をその成
形性の許す限り、できるだけ多量に配合する必要があ
る。
Semiconductors and electronic parts are sealed with a ceramic package or resin to protect them from the external environment, but this sealing material is a synthetic material containing an inorganic filler in terms of cost, productivity, etc. Resin compositions are widely used. This synthetic resin composition is composed of a thermosetting resin such as an epoxy resin and an inorganic filler such as silica, but these compositions have a small coefficient of thermal expansion, good thermal conductivity and low moisture permeability. Since it is desirable that the inorganic wet filler has excellent mechanical properties and the like and that the cost is low, it is necessary to blend the inorganic wet filler as much as possible, as long as the moldability thereof allows.

【0003】 しかしながら、充填剤として用いる無機
質粉末は主としてその塊状物を、適度の大きさと分布を
持った粉末に粉砕するため、その形状は一般に角を持っ
ており、これとエポキシ樹脂等の熱硬化性樹脂を混合し
て封止材料とする場合その流動性が十分ではなく、充填
性や作業性が悪いうえ、成型加工工程の装置類を著しく
摩耗するという欠点を持っていた。また充填剤粒子の鋭
くとがった角が半導体素子表面を傷つけ、そのことがソ
フトエラーを引き起こす原因となるとの報告も出されて
いる。
However, since the inorganic powder used as a filler mainly pulverizes the lumps thereof into powder having a proper size and distribution, its shape generally has corners, and this and thermosetting of epoxy resin or the like. When a resin mixture is used as a sealing material, the fluidity is not sufficient, the filling property and the workability are poor, and the devices in the molding process are significantly worn. It has also been reported that the sharp and sharp corners of the filler particles damage the surface of the semiconductor device, which causes a soft error.

【0004】 一般に熱硬化性樹脂が硬化する際に収縮
することにより応力が生じるが、この応力のほか半導体
から発生する熱により、半導体素子と封止樹脂組成物の
熱膨張係数の差が大きいために生ずる応力が存在する。
これらの内部応力のうち、後者の応力を緩和するため
に、通常熱膨張率の小さい無機質充填剤を、出来るだけ
多量に充填することが望ましい。しかしながらこの面に
おいても粉砕によって製造される、角ばった充填剤では
充填量を増やすと、極端に流動性が低下するため、量的
に制約を受けざるを得ず、内部応力の緩和には役立たな
い。
In general, when the thermosetting resin is contracted when it is cured, stress is generated, and in addition to this stress, the heat generated from the semiconductor causes a large difference in thermal expansion coefficient between the semiconductor element and the encapsulating resin composition. There is a stress that occurs in.
Of these internal stresses, in order to relieve the latter stress, it is usually desirable to fill an inorganic filler having a small coefficient of thermal expansion as much as possible. However, in this respect as well, if the filling amount of the angular filler produced by pulverization is increased, the fluidity is extremely reduced, so that there is no choice but to be limited by the amount, and it is not useful for relaxing internal stress. .

【0005】 このような問題点を解決するため、例え
ば、特開昭58−145613号公報または、特開昭6
1−118131号公報によれば、結晶微粉末シリカを
ガス流と共にノズルから噴出させ、粒子の分散、溶融、
冷却等の適当な条件に制御して、球状の溶融微粉末シリ
カをつるる方法が提案されている。しかしながら、この
方法はコストが高くなる欠点を有する。
In order to solve such problems, for example, JP-A-58-145613 or JP-A-6-
According to Japanese Patent Laid-Open No. 1-118131, crystalline fine powder silica is ejected from a nozzle together with a gas flow to disperse and melt particles.
A method has been proposed in which spherical fused fine powder silica is suspended by controlling appropriate conditions such as cooling. However, this method has the drawback of being costly.

【0006】 一方、結晶タイプの球状シリカの製造例
は、現在まで提案されていない。 このような状況に鑑みて、本発明者らは丸味を帯びたシ
リカ微粉末粒子の製造法について検討し、特開昭63−
282109号公報(シリカ微粉末粒子の製造方法)と
して昭和62年5月13日に出願した。特開昭63−2
82109号公報の方法によって得られるシリカ微粉末
は、最大粒子径が300μm以下の丸味を帯びた粒子
で、半導体素子封止用合成樹脂組成物の充填剤としてす
ぐれたものである。
On the other hand, no production example of crystal-type spherical silica has been proposed so far. In view of such a situation, the present inventors have investigated a method for producing roundish silica fine powder particles, and disclosed in JP-A-63-63
The application was filed on May 13, 1987 as Japanese Patent No. 282109 (method for producing fine silica powder particles). JP-A-63-2
The fine silica powder obtained by the method of Japanese Patent No. 82109 is a rounded particle having a maximum particle diameter of 300 μm or less, and is an excellent filler for a synthetic resin composition for encapsulating a semiconductor element.

【0007】その後本発明者らが鋭意、検討を続けたと
ころ、最大粒子径が200μm以下で、平均粒子径が7
μm以上35μm以下、かつ、微粒子シリカの含有量が
3μm以下のものを12重量%以上、1μm以下のもの
を2重量%以上含有するシリカ微粉末が充填剤等として
よりすぐれた特性を持つことを知り、本発明に到達し
た。
[0007] The inventors of the present invention then continued to make a thorough study, and found that the maximum particle diameter was 200 μm or less and the average particle diameter was 7 μm.
A fine silica powder containing 12% by weight or more of particles having a fine silica content of 3 μm or less and 2% by weight or more of particles having a fine silica content of 3 μm or less has excellent properties as a filler or the like. Knowing, I arrived at the present invention.

【0008】[0008]

【課題を解決するための手段】[Means for Solving the Problems]

本発明者らは前記課題を解決するために鋭意検討した結
果、本発明を完成するな至った。 即ち、本発明の要旨は粉砕状シリカに外部から押圧力を
加えながら水系媒体存在下で粒子同志を摩砕することに
よって得られる、粒子の角がない、丸味をおびたシリカ
微粉末であって、最大粒子径が200μm以下で平均粒
子径が7μm以上35μm以下であり、かつ3μm以下
の微粒子シリカが12重量%以上、1μm以下の微粒子
シリカが2重量%以上の粒度分布を有するシリカ微粉末
に関するものであり、本発明のシリカ微粉末を熱硬化性
樹脂に配合する良好な流動性を付与するとともに高配合
をも可能にするものである。
As a result of intensive studies to solve the above-mentioned problems, the present inventors have completed the present invention. That is, the gist of the present invention is a finely powdered silica having rounded corners, which is obtained by grinding particles of each other in the presence of an aqueous medium while applying a pressing force to the ground silica from the outside. A fine silica powder having a maximum particle diameter of 200 μm or less, an average particle diameter of 7 μm or more and 35 μm or less, and a fine particle silica of 3 μm or less having a particle size distribution of 12% by weight or more and 1 μm or less of 2% by weight or more. The present invention provides good flowability when the silica fine powder of the present invention is blended with a thermosetting resin, and enables high blending.

【0009】 本発明に用いる破砕状シリカは、結晶シ
リカ、溶融シリカのいずれでも構わず、結晶シリカとし
ては一般に天然の高純度の珪石、珪砂、水晶等が用いら
れ、溶融シリカは、これら結晶シリカを高温で溶融して
インゴットにしたものである。通常これらをジョークラ
ッシャー、ロールクラッシャー等で粗砕し、これら粗砕
品をさらにボールミル等で微粉砕し、破砕状シリカとし
て本発明に用いる。 ここで得られる破砕状微粉砕シリカの平均粒子径は、最
終製品の角をとって丸味をおびたシリカ微粉末のそれよ
りもやや大きくしておく必要がある。
The crushed silica used in the present invention may be either crystalline silica or fused silica. As the crystalline silica, natural high-purity silica stone, silica sand, quartz or the like is generally used. Is an ingot obtained by melting at a high temperature. Usually, these are roughly crushed with a jaw crusher, a roll crusher, etc., and these coarsely crushed products are further finely crushed with a ball mill etc., and used as crushed silica in the present invention. The average particle size of the crushed finely pulverized silica obtained here needs to be slightly larger than that of the fine silica powder having the rounded corners of the final product.

【0010】 本発明のシリカ微粉末は、熱硬化性樹脂
と配合すると流動性が著しく良くなるのであるが、その
作用機構は明確ではない。しかし、粒子の角がとれ丸く
なることのほかに、摩砕の結果生成したサブミクロンオ
ーダーの粒子を含む微粒子が、数十ミクロンオーダーの
粒子に付着して流動性が改善され、最適な粒度分布を形
成するために大いに貢献しているものと考えられる。
When the silica fine powder of the present invention is blended with a thermosetting resin, the fluidity is remarkably improved, but its action mechanism is not clear. However, in addition to the rounded corners of the particles, fine particles containing sub-micron-order particles generated as a result of grinding adhere to particles of the order of tens of microns, improving the fluidity, which results in an optimal particle size distribution. It is believed that they have made a great contribution to the formation of.

【0011】 本発明において、角とり処理は破砕シリ
カに外部から押圧力を加えながら、水系媒体存在下で粒
子同志を摩砕するが、水系媒体が存在しないと押圧力が
粉体に円滑に伝達されず、摩砕の効率は極めて低くな
る。通常破砕状シリカに対して0.5〜18重量%、好
ましくは3〜13重量%の水系媒体の存在が、摩砕に対
して有効に作用する。 使用する水系媒体としてはシリカ微粒子同志が相互に作
用しあい、外部から粉体への圧力が伝達し易い液体であ
ればよく、水、アルコール類、鉱油等の液状物質が有利
に使用できるが、媒体のコスト、操作等の取扱い易さ、
操作後の分離し易さなどから、水単独、または水にエタ
ノール、メタノール等のアルコール類を溶かした媒体が
工業的に最も有利に使用できる。
In the present invention, the chamfering treatment grinds particles together in the presence of an aqueous medium while applying a pressing force from the outside to the crushed silica, but the pressing force is smoothly transmitted to the powder in the absence of the aqueous medium. Not being done, the efficiency of milling is very low. The presence of 0.5-18% by weight, preferably 3-13% by weight, of the aqueous medium, relative to the normally crushed silica, effectively acts on the attrition. As the aqueous medium to be used, it is sufficient that the silica fine particles interact with each other and the pressure from the outside is easily transmitted to the powder, and water, alcohols, liquid substances such as mineral oil can be advantageously used, but the medium Cost, ease of handling, etc.,
From the viewpoint of ease of separation after the operation, water alone or a medium in which alcohols such as ethanol and methanol are dissolved in water can be industrially most advantageously used.

【0012】 また、外部からローラーに加える押圧力
であるが、機械により押圧の仕方が異なるので数値的に
限定できないが、押圧力が余り強い場合、角とりのみな
らず粒子の体積破壊がおき、粉砕が進行し角とり処理が
阻害される。また、余り弱い場合、角とりの効率が低下
してくるので、機器、原料、品種(結晶質、非結晶)等
に応じて、適切に決めればよい。また、数mm以下の粗
砕品を直接この角とり工程に送って、所望粒度への粉砕
と同時に角とり操作をおこなうこともできる。 このように外部から押圧力を加えながら粒子どうしを摩
砕する手段には種々の方法があるが、エネルギーなどの
コストあるいは効率性の面からみてローラーミルが最も
有効に使用できる。
Further, the pressing force applied to the roller from the outside cannot be numerically limited because the pressing method differs depending on the machine, but when the pressing force is too strong, not only the chamfering but also the volume destruction of the particles occurs, The crushing progresses and the chamfering process is hindered. If it is too weak, the efficiency of chamfering will decrease, so it may be appropriately determined according to the equipment, raw material, product type (crystalline or amorphous), and the like. Further, it is also possible to send a coarsely crushed product having a size of several mm or less directly to this chamfering step, and perform the chamfering operation simultaneously with the pulverization to a desired particle size. As described above, there are various methods for grinding the particles while applying a pressing force from the outside, but the roller mill can be most effectively used from the viewpoint of cost such as energy or efficiency.

【0013】 本発明のシリカ微粉末は最大粒子径が2
00μm以下、好ましくは100μm以下であり、20
0μm以上であると、半導体の樹脂封止の工程でつまり
生ずるため使用できない。更に平均粒子径は7μm以上
35μm以下、好ましくは12μm以上20μm以下で
あり、7μm以下であっても35μm以上であっても、
いずれも樹脂組成物の良好な流動性が損なわれる。
The fine silica powder of the present invention has a maximum particle size of 2
00 μm or less, preferably 100 μm or less, 20
If it is 0 μm or more, it cannot be used because it occurs in the step of resin sealing the semiconductor. Further, the average particle size is 7 μm or more and 35 μm or less, preferably 12 μm or more and 20 μm or less, and 7 μm or less or 35 μm or more,
In either case, the good fluidity of the resin composition is impaired.

【0014】 次に微粒子シリカの粒度分布であるが、
3μm以下のものが12重量%以上好ましくは14重量
%以上、1μm以下のものが2重量%以上好ましくは3
重量%以上存在すると、良好な流動性が得られる。但
し、3μm以下の微粒子は必ずしも角をとって丸味をお
びる必要はなく破砕状微粒子でも良い。いずれの場合も
下限値より少ない存在量では、樹脂組成物の流動性は低
下してくる。上記、7〜35μmの平均粒子径及び、所
望の割合で微粒子が存在するシリカ微粉末は、押圧力あ
るいは、回転数、水系媒体の量等を適宜調節することに
より得ることができるし、また、3μm以下の破砕状シ
リカを本処理前または途中に、または処理後に加えても
得ることができる。
Next, regarding the particle size distribution of fine particle silica,
Those having a thickness of 3 μm or less are 12% by weight or more, preferably 14% by weight or more, and those having a thickness of 1 μm or less are 2% by weight or more, preferably 3
When it is present in an amount of not less than wt%, good fluidity can be obtained. However, fine particles of 3 μm or less do not necessarily have to be rounded to have roundness, and may be crushed fine particles. In any case, if the amount is less than the lower limit, the fluidity of the resin composition will decrease. The above-mentioned silica fine powder having an average particle diameter of 7 to 35 μm and fine particles present in a desired ratio can be obtained by appropriately adjusting the pressing force, the rotation speed, the amount of the aqueous medium, or the like. It can also be obtained by adding crushed silica of 3 μm or less before or during the main treatment or after the treatment.

【0015】 本発明のシリカ微粉末は熱硬化性樹脂に
配合させて使用することができる。熱硬化性樹脂として
は、エポキシ樹脂、フェノール樹脂、ポリエステル樹
脂、シリコーン樹脂等のいずれの樹脂も使用できるが、
この中でエポキシ樹脂が工業的に有利に用いることが出
来る。これらの熱硬化性樹脂100重量部に、本発明の
シリカ微粉末を60〜600重量部の範囲で配合すると
所望の樹脂組成物が得られる。60重量部以下では、内
部応力低下の効果がみられず、600重量部をこえる
と、樹脂の流動性が低下するので好ましくない。熱硬化
性樹脂に微粉末を混練する方法としては、通常ニーダ
ー、ロールミル、ミキサー等を用いればよい。
The silica fine powder of the present invention can be used by being mixed with a thermosetting resin. As the thermosetting resin, any resin such as epoxy resin, phenol resin, polyester resin, silicone resin can be used,
Of these, epoxy resins can be industrially advantageously used. A desired resin composition can be obtained by blending 100 parts by weight of these thermosetting resins with the fine silica powder of the present invention in the range of 60 to 600 parts by weight. If it is 60 parts by weight or less, the effect of reducing the internal stress is not observed, and if it exceeds 600 parts by weight, the fluidity of the resin is lowered, which is not preferable. As a method of kneading the fine powder with the thermosetting resin, a kneader, a roll mill, a mixer or the like may be usually used.

【0016】[0016]

【実施例】【Example】

次に本発明を実施例により、詳細に説明する。 実施例1 粗砕結晶シリカをボールミルにより微粉砕し、平均粒子
径23.2μmの破砕状結晶シリカ500gを得た。こ
れをローラーミル(MPV−0.5型松本鋳造鉄工所
製)に仕込み、同時に水60mlを添加した。ローラー
の押圧力40kg/cm(線圧)、ローラーと底板と
のクリアランス3mm、底板の回転数を42rpmに設
定して、1時間処理した。得られた処理物の乾燥、粉砕
した結果、平均粒子径は19.4μmで、微粒子の粒度
分布は3μm以下22.1重量%、1μm以下4.4重
量%であった。なお粒度分布の測定はレーザー回折式粒
度分布測定装置(CILAS、モデル715)を用いて
行った。このようにして角とり処理を行って製造された
シリカ微粉末の電子顕微鏡写真を図1に示した。
Next, the present invention will be described in detail with reference to examples. Example 1 The coarsely crushed crystalline silica was finely crushed by a ball mill to obtain 500 g of crushed crystalline silica having an average particle diameter of 23.2 μm. This was charged into a roller mill (MPV-0.5 type Matsumoto Foundry Iron Works), and 60 ml of water was added at the same time. The pressing force of the roller was 40 kg / cm 2 (linear pressure), the clearance between the roller and the bottom plate was 3 mm, and the number of rotations of the bottom plate was 42 rpm. As a result of drying and pulverizing the obtained treated product, the average particle diameter was 19.4 μm, and the particle size distribution of the fine particles was 3 μm or less 22.1% by weight and 1 μm or less 4.4% by weight. The particle size distribution was measured using a laser diffraction type particle size distribution measuring device (CILAS, model 715). An electron micrograph of the silica fine powder produced by performing the chamfering treatment in this manner is shown in FIG.

【0017】 実施例2 実施例1で用いた破砕状結晶シリカの平均粒子径および
ローラーミルの処理条件を変えて、表1のA、B、Cに
示し角とり処理を行ったシリカ微粉末を製造した。
Example 2 By changing the average particle size of the crushed crystalline silica used in Example 1 and the treatment conditions of the roller mill, the silica fine powders shown in Tables A, B, and C and subjected to the chamfering treatment were used. Manufactured.

【表1】 [Table 1]

【0018】 比較例1 実施例2と同様にして、破砕状結晶シリカを用いて角と
り処理を行った表2のD、Eに示すシリカ微粉末を製造
した。
Comparative Example 1 In the same manner as in Example 2, finely powdered silica shown in D and E of Table 2 was produced by subjecting the crushed crystalline silica to a chamfering treatment.

【表2】 [Table 2]

【0019】 比較例2 珪石の粗砕品をボールミルにて微粉砕し、平均粒子径1
9.2μmの破砕状結晶シリカを得た。このものは、ロ
ーラーミルで処理をしていないため、粒子に角があり、
電子顕微鏡写真は、図2に示す如くであった。また微粒
子の粒度分布は、3μm以下12.4重量%、1μm以
下2.0重量%であった。
Comparative Example 2 A coarsely crushed silica stone was finely pulverized with a ball mill to give an average particle diameter of 1
Crushed crystalline silica of 9.2 μm was obtained. Since this one is not processed with a roller mill, the particles have corners,
The electron micrograph was as shown in FIG. The particle size distribution of the fine particles was 3 μm or less, 12.4% by weight, and 1 μm or less, 2.0% by weight.

【0020】 実施例3 粗砕溶融シリカをボールミルにより微粉砕し、平均粒子
径24.6μm破砕状溶融シリカ500gを得た。以後
ローラーの押圧力を20kg/cm(線圧)に変えた
以外は実施例1と同様に角とり処理して、平均粒子径1
8.6μm、微粒子の粒度分布は3μm以下23.2重
量%、1μm以下4.1重量%のシリカ微粉末を得た。
Example 3 Coarse crushed fused silica was finely crushed with a ball mill to obtain 500 g of crushed fused silica having an average particle diameter of 24.6 μm. After that, the chamfering treatment was performed in the same manner as in Example 1 except that the pressing force of the roller was changed to 20 kg / cm 2 (linear pressure), and the average particle size was 1
A silica fine powder having a particle size distribution of 8.6 μm and a fine particle size distribution of 3 μm or less and 23.2% by weight and 1 μm or less and 4.1% by weight was obtained.

【0021】 比較例3 比較例2と同様にして溶融シリカ粗砕品をローラーミル
で角とり処理をせず、単にボールミルで微粉砕して平均
粒子径18.5μmの破砕状溶融シリカを得た。このも
のの微粒子の粒度分布は3μm以下16.2重量%、1
μm以下3.1重量%であった。
Comparative Example 3 In the same manner as in Comparative Example 2, the fused silica coarsely crushed product was not finely chamfered by a roller mill but was simply finely pulverized by a ball mill to obtain crushed fused silica having an average particle diameter of 18.5 μm. . The particle size distribution of fine particles of this product is 3 μm or less 16.2% by weight, 1
It was 3.1% by weight or less of μm.

【0022】 試験例1〜5 実施例1〜2で製造した微粉末(破砕状結晶シリカをロ
ーラーミルで処理して得たもの。)をエポキシ樹脂10
0重量部に対し、表3に示す重量部を配合し、ニーダー
にて15分混練後冷却、粉砕し、エポキシ樹脂組成物を
得た。これらの組成物の流動性を見るため、EMMI規
格1−66に基いてスパイラルフローを測定した。
Test Examples 1 to 5 The fine powder (obtained by treating crushed crystalline silica with a roller mill) produced in Examples 1 and 2 was used as an epoxy resin 10.
To 0 part by weight, the parts by weight shown in Table 3 were blended, kneaded in a kneader for 15 minutes, cooled and pulverized to obtain an epoxy resin composition. To see the flowability of these compositions, spiral flow was measured according to EMMI standard 1-66.

【表3】 [Table 3]

【0023】 比較試験例1〜3 比較例1D、1E及び比較例2で得た結晶シリカ微粒子
を充填剤を用いて、試験例1〜5と同様にしてエポキシ
樹脂組成物を得た(表4)。1μm以下のシリカ微粉末
が2重量%以下であったり、平均粒子径が小さ過ぎた
り、あるいは充填剤に角があったりした条件では流動性
が悪くなることが明らかとなった。
Comparative Test Examples 1 to 3 Epoxy resin compositions were obtained in the same manner as in Test Examples 1 to 5 using the crystalline silica fine particles obtained in Comparative Examples 1D, 1E and Comparative Example 2 as a filler (Table 4). ). It was clarified that the fluidity was deteriorated under the condition that the silica fine powder having a particle size of 1 μm or less was 2% by weight or less, the average particle size was too small, or the filler was angular.

【表4】 [Table 4]

【0024】 実施例6、7 破砕状溶融シリカをローラーミルで角とり処理する実施
例3の方法で得た溶融シリカ微粒子を充填剤として用
い、試験例1〜5と同様にしてエポキシ樹脂と配合し、
表5に示すエポキシ樹脂組成物を得、同時にスパイラル
フローを測定した。
Examples 6 and 7 Blended with an epoxy resin in the same manner as in Test Examples 1 to 5 using the fused silica fine particles obtained by the method of Example 3 in which the crushed fused silica is cut off with a roller mill as a filler. Then
The epoxy resin compositions shown in Table 5 were obtained, and at the same time, the spiral flow was measured.

【0025】 比較試験例4 比較試験例4は破砕状溶融シリカをローラーミルで角と
り処理しないままのものを充填として用いた場合であ
る、結晶シキラ微粒子における比較試験例1〜3の場合
と同じように、溶融シリカ微粒子を用いた場合も、表5
に示すように流動性の低下が見られた。
Comparative Test Example 4 Comparative Test Example 4 is the same as the case of Comparative Test Examples 1 to 3 in the case of fine crystalline silica particles, in which crushed fused silica was used as a filling without being chamfered by a roller mill. Similarly, when the fused silica fine particles are used, Table 5
As shown in, the liquidity was reduced.

【表5】 [Table 5]

【0026】 参考例 実施例1、比較例2、実施例3、比較例3で得られた微
粉末を各々70重量%の割合で含有するエポキシ樹脂組
成物を製造し、これらを50mmφの金型に充填して加
圧成型し、外径50mm、高さ10mmのタブレットを
作製した。これを用いて摩耗試験を実施した。結果を図
3、図4に示した。本発明の角をとり、丸味をおびたシ
リカ微粒子を充填剤に用いた場合、明らかに摩耗性が改
善されていた。
Reference Example An epoxy resin composition containing 70% by weight of each of the fine powders obtained in Example 1, Comparative Example 2, Example 3, and Comparative Example 3 was produced, and these were molded in a mold of 50 mmφ. Was filled in and was pressure-molded to produce a tablet having an outer diameter of 50 mm and a height of 10 mm. A wear test was carried out using this. The results are shown in FIGS. 3 and 4. When the rounded and rounded silica fine particles of the present invention were used as the filler, the wear property was clearly improved.

【0027】[0027]

【発明の効果】【The invention's effect】

本発明のシリカ微粉末は、熱効果性樹脂に配合して半導
体等の電子部品の封止に用いた場合、トランスファー成
型工程における流動性、摩耗性が改善されるうえ、封止
物の内部応力の低下にも役立ち、作業性、性能の両面で
改善をはかることができる。
The silica fine powder of the present invention, when mixed with a heat-effective resin and used for sealing electronic components such as semiconductors, improves the fluidity and abrasability in the transfer molding process, and also increases the internal stress of the sealed product. It is also useful in reducing workability and improving workability and performance.

【図面の簡単な説明】[Brief description of drawings]

【図1】角をとり、丸味を帯びた本発明における破砕状
結晶シリカ微粒子の結晶構造を示す電子顕微鏡写真であ
る。
FIG. 1 is an electron micrograph showing a crystal structure of crushed crystalline silica fine particles having rounded corners and roundness according to the present invention.

【図2】処理前の角のある破砕状結晶シリカ微粒子の結
晶構造を示す顕微鏡写真である。
FIG. 2 is a photomicrograph showing the crystal structure of crushed crystalline silica fine particles with corners before treatment.

【図3】実施例1または比較例2により得られた微粉末
を配合して得られたエポキシ樹脂組成物のtaber摩
耗試験の結果を示す。
FIG. 3 shows the results of a taber abrasion test of an epoxy resin composition obtained by blending the fine powder obtained in Example 1 or Comparative Example 2.

【図4】実施例3または比較例3により得られた微粉末
を配合して得られたエポキシ樹脂組成物のtaber摩
耗試験を結果を示す。
FIG. 4 shows the results of a taber abrasion test of an epoxy resin composition obtained by blending the fine powder obtained in Example 3 or Comparative Example 3.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】破砕状シリカに外部から押圧力を加えなが
ら水系媒体存在下で粒子同志を摩砕することによって得
られる、粒子の角がない、丸味をおびたシリカ微粉末で
あって、最大粒子径が200μm以下で平均粒子径が7
μm以上35μm以下であり、かつ3μm以下の微粒子
シリカが12重量%以上、1μm以下の微粒子シリカが
2重量%以上の粒度分布を有するシリカ微粉末。
1. A finely powdered silica having rounded corners, which is obtained by grinding particles together in the presence of an aqueous medium while applying a pressing force to the crushed silica from the outside. Particle size is less than 200 μm and average particle size is 7
A fine silica powder having a particle size distribution of 12% by weight or more and 2% by weight or more of 12% by weight or more of finely divided silica having a size of 3 μm or less and 3 μm or less.
【請求項2】破砕状シリカ外部から押圧力を加えながら
水系媒体存在下で粒子同志を摩砕する方法が、ローラー
ミルを用いて行う方法である請求項1記載のシリカ微粉
末。
2. The silica fine powder according to claim 1, wherein the method of grinding the particles in the presence of an aqueous medium while applying a pressing force from the outside of the crushed silica is a method using a roller mill.
【請求項3】破砕状シリカが結晶シリカ及び/又は溶融
シリカである請求項1記載のシリカ微粉末。
3. The fine silica powder according to claim 1, wherein the crushed silica is crystalline silica and / or fused silica.
JP2416152A 1990-12-31 1990-12-31 Silica fine powder Expired - Lifetime JPH062569B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2416152A JPH062569B2 (en) 1990-12-31 1990-12-31 Silica fine powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2416152A JPH062569B2 (en) 1990-12-31 1990-12-31 Silica fine powder

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP22166887A Division JPS6462362A (en) 1987-09-03 1987-09-03 Filler and polymer composition containing same

Publications (2)

Publication Number Publication Date
JPH03247635A JPH03247635A (en) 1991-11-05
JPH062569B2 true JPH062569B2 (en) 1994-01-12

Family

ID=18524393

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2416152A Expired - Lifetime JPH062569B2 (en) 1990-12-31 1990-12-31 Silica fine powder

Country Status (1)

Country Link
JP (1) JPH062569B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114163691B (en) * 2021-11-12 2023-03-28 联瑞新材(连云港)有限公司 Silica micro powder filler composition for high-thermal-conductivity high-fluidity EMC and preparation method thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5829858A (en) * 1981-08-13 1983-02-22 Nitto Electric Ind Co Ltd Resin composition for sealing electronic component
JPS58138740A (en) * 1982-02-15 1983-08-17 Denki Kagaku Kogyo Kk Resin composition
JPS5922955A (en) * 1982-07-29 1984-02-06 Toshiba Chem Corp Resin composition for sealing semiconductor
JPH0651786B2 (en) * 1985-09-30 1994-07-06 株式会社東芝 Epoxy resin composition for semiconductor device encapsulation
JPS6296567A (en) * 1985-10-24 1987-05-06 Denki Kagaku Kogyo Kk Semiconductor sealing resin composition
JPS6462362A (en) * 1987-09-03 1989-03-08 Seitetsu Kagaku Co Ltd Filler and polymer composition containing same
JPH0528744A (en) * 1991-07-24 1993-02-05 Canon Inc Image recording device and application unit detachable from the image recording device

Also Published As

Publication number Publication date
JPH03247635A (en) 1991-11-05

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