JPS6296310A - Production of fused silica spherule - Google Patents

Production of fused silica spherule

Info

Publication number
JPS6296310A
JPS6296310A JP60236367A JP23636785A JPS6296310A JP S6296310 A JPS6296310 A JP S6296310A JP 60236367 A JP60236367 A JP 60236367A JP 23636785 A JP23636785 A JP 23636785A JP S6296310 A JPS6296310 A JP S6296310A
Authority
JP
Japan
Prior art keywords
slurry
fine powder
fused silica
water
spherules
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.)
Pending
Application number
JP60236367A
Other languages
Japanese (ja)
Inventor
Tatsuro Iida
達郎 飯田
Hiroyuki Kuroda
黒田 寛之
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP60236367A priority Critical patent/JPS6296310A/en
Publication of JPS6296310A publication Critical patent/JPS6296310A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L23/00Details of semiconductor or other solid state devices
    • H01L23/28Encapsulations, e.g. encapsulating layers, coatings, e.g. for protection
    • H01L23/29Encapsulations, e.g. encapsulating layers, coatings, e.g. for protection characterised by the material, e.g. carbon
    • H01L23/293Organic, e.g. plastic
    • H01L23/295Organic, e.g. plastic containing a filler
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L2924/00Indexing scheme for arrangements or methods for connecting or disconnecting semiconductor or solid-state bodies as covered by H01L24/00
    • H01L2924/0001Technical content checked by a classifier
    • H01L2924/0002Not covered by any one of groups H01L24/00, H01L24/00 and H01L2224/00

Abstract

PURPOSE:To readily produce fused silica spherules without sticking of fine powder, by jetting powdery silica together with a high-temperature flame, flame, adding water to the resultant spherules to form a slurry, adjusting the slurry to a proper pH and stirring the adjusted slurry. CONSTITUTION:Powdery silica obtained by pulverizing quartzite, etc., together with a high-temperature flame, e.g. propane/oxygen flame, etc., is jetted, fused and spherized. Water free of impurities, e.g. ion exchange water or distilled water, etc., is added to the resultant fused silica spherules with sticking fine powder to form a slurry, which is preferably adjusted to 6-9pH by adding aqueous ammonia, etc., and 20-50wt% concentration thereof. The fine powder is then separated while stirring the above-mentioned slurry and further removed. Thereby, the aimed fused silica spherules having a small specific surface area without sticking of fine powder are obtained.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は半導体などの電子部品の封止材料あるいは化粧
料等に用いられる溶融シリカ球状体の製造法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing fused silica spheres used in sealing materials for electronic components such as semiconductors, cosmetics, and the like.

(従来の技術) 浴融シリカ球状体は低熱膨張性、熱伝導性、電気絶縁性
に加えて、球状であるために外部接触物への損傷が少な
いという利点を有しており、それ故、工CXLSI等の
粘密な電子部品の封止材料や化粧料への使用が期待され
ている。
(Prior Art) In addition to low thermal expansion, thermal conductivity, and electrical insulation, bath-fused silica spheres have the advantage of causing less damage to external contact objects because of their spherical shape. It is expected to be used as a sealing material for sticky electronic components such as CXLSI and in cosmetics.

従来、溶融シリカ球状体の製造方法は珪石、珪砂、水晶
等あるいはハロゲン化珪素化合物から熱分解等により得
られた粉末を溶融し塊状にしたものを、粉砕し、プロパ
ン/酸素炎等の高温火炎と共に噴出することにより溶融
・球状化する方法が一般的である。
Conventionally, fused silica spheres have been produced by melting powder obtained by thermal decomposition from silica stone, silica sand, quartz, etc. or silicon halide compounds, pulverizing it into a lump, and then pulverizing it into a lump using a high-temperature flame such as a propane/oxygen flame. A common method is to melt and form spheres by ejecting them together.

(発明が解決しようとする問題点) しかしながら以上の様な方法で製造された溶融シリカ球
状体はその表面に1μm未満の微粉が多数付着している
のが認められ、特に44μm以下の球状体表面への付着
が著しい。この微粉は、粉末シリカが高温火炎中を通過
する際に、熱による破砕が起きて生成する、あるいは粉
末シリカ表面から810のガスが蒸発しそれが凝縮固化
して生成すると考えられている。
(Problems to be Solved by the Invention) However, it has been observed that the fused silica spheres produced by the method described above have a large number of fine particles of less than 1 μm attached to their surfaces, especially the surfaces of the spheres of 44 μm or less. Significant adhesion to. It is believed that this fine powder is generated when powdered silica is crushed by heat when it passes through a high-temperature flame, or when 810 gas evaporates from the surface of the powdered silica and is condensed and solidified.

溶融シリカ球状体の表面にこの様な微粉が多数付着して
いることは、球状体としての特性を損うだけでなく、比
表面積の増大を招きこれが光填剤として組成物に官有し
たときの組成物の流動性、加工性の悪化の原因になる。
The presence of a large number of such fine powders on the surface of the fused silica spheres not only impairs the properties of the spheres, but also increases the specific surface area, and when incorporated into the composition as an optical filler. This causes deterioration of the fluidity and processability of the composition.

本発明は微粉の付着がない溶融シリカ球状体の製造方法
を提供することを目的とする。
An object of the present invention is to provide a method for producing fused silica spheres without adhesion of fine powder.

(問題点を解決するたぬの手段) 本発明者らは粉末シリカを高温火炎とともに噴射して得
られる溶融シリカ球状体を水洗することにより微粉を分
離・除去する方法について種々検討した。その結果、シ
リカ球状体スラリーの−が微粉の分離の容易さに関係し
、スラリー−が6〜9の範囲において微粉が容易に分離
されることを見出し本発明に到った。
(Unprecedented Means to Solve the Problem) The present inventors have studied various methods for separating and removing fine powder by washing with water fused silica spheres obtained by injecting powdered silica together with high-temperature flame. As a result, it was discovered that the - of the silica sphere slurry is related to the ease of separation of fine powder, and that fine powder is easily separated when the slurry has a - of 6 to 9.

すなわち、本発明は、粉末シリカを高温火炎と共に噴射
して得られた微粉付着の溶融シリカ球状体に、水を加え
てスラリーとし、スラリーのpHを6〜9に調整して攪
拌を行ないながら微粉を分離しそれを除去することを特
徴とする溶融シリカ球状体の製造方法である。
That is, in the present invention, water is added to a fused silica sphere with fine powder attached to it obtained by injecting powdered silica together with a high-temperature flame to form a slurry, the pH of the slurry is adjusted to 6 to 9, and the fine powder is mixed while stirring. This is a method for producing fused silica spheres, characterized by separating and removing the fused silica spheres.

以下、更に詳しく本発明について説明する。The present invention will be explained in more detail below.

本発明において浴融シリカ球状体は通常の珪石、珪砂、
水晶、あるいはハロゲン化珪素化合物から熱分解により
生成する粉末シリカを高温火炎とともに噴射して得られ
るものであり、その表面にはシリカの微粉末が付着して
いるのである。
In the present invention, the bath-fused silica spheres are ordinary silica stone, silica sand,
It is obtained by injecting powdered silica produced by thermal decomposition from quartz or a silicon halide compound with high-temperature flame, and fine silica powder is attached to the surface.

本発明において使用される水は溶融シリカ球状体の用途
を考慮するとイオン交換水、蒸留水等の不純物を除去し
た水であることが好ましい。
Considering the use of the fused silica spheres, the water used in the present invention is preferably water from which impurities have been removed, such as ion-exchanged water or distilled water.

スラリーの濃度については、処理する溶融シリカ球状体
の粒度に応じて適宜変えられるべきものであるが20〜
50重!に%が適当である。
The concentration of the slurry should be changed as appropriate depending on the particle size of the fused silica spheres to be treated;
50 weight! % is appropriate.

該溶融シリカ球状体に水を加えるとシリカ表面のシラノ
ール基のために酸性(p)13〜4)になる。
When water is added to the fused silica sphere, it becomes acidic (p) 13-4) due to the silanol groups on the silica surface.

そこで希薄なアンモニア水、陰イオン系の界面活性剤等
を加えてpHを6〜9に調整する。−が6未満または9
を越えると微粉分離の効果が低い。
Then, dilute ammonia water, an anionic surfactant, etc. are added to adjust the pH to 6-9. - is less than 6 or 9
If it exceeds , the effect of fine powder separation will be low.

攪拌装置はスラリーを急速に振盪できるものであれば何
でもよいが、サンドミル、ボールミル、コロイドミル、
アトライターなど高速の水流を発生させる装置が望まし
い。このような装置によりスラリーを急速に攪拌してシ
リカ球状体から微粉を分離し、ついで静置沈降槽、液体
サイクロン等の装置により微粉を含む上溌液を分離する
ことにより、微粉を除去することができる。
Any stirring device that can rapidly shake the slurry may be used, such as a sand mill, ball mill, colloid mill,
A device that generates high-speed water flow, such as an attritor, is desirable. The fine powder is removed by rapidly stirring the slurry using such a device to separate the fine powder from the silica spheres, and then separating the supernatant liquid containing the fine powder using a device such as a static sedimentation tank or a liquid cyclone. I can do it.

(実施例) 次に本発明を実施例により更に詳しく説明する。(Example) Next, the present invention will be explained in more detail with reference to Examples.

実施例1〜5および比較例1〜6 高純度水晶をボールミルで粉砕し44μm以下に粒度調
整したものを、LPG/酸素の火炎中に10ky/hで
連続的に供給し溶融球状化を行なった。系内の各捕集部
のうち、サイクロン及びバグフィルタ−から回収された
溶融シリカ球状体の粒度分布及び比表面積を第1表に示
す。
Examples 1 to 5 and Comparative Examples 1 to 6 High-purity quartz crystals were ground with a ball mill and adjusted to a particle size of 44 μm or less, and were continuously fed into an LPG/oxygen flame at 10 ky/h to melt and spheroidize them. . Table 1 shows the particle size distribution and specific surface area of the fused silica spheres recovered from the cyclone and bag filter among the collection sections in the system.

この溶融シリカ球状体にイオン交換水を加え第2表に示
すスラリー濃度とした6 1%アンモニア水を加えて第
2表に示す−に調整し、サンドミルにより30分間攪拌
を行ない続いて液体サイクロンで微粉を分級除去した。
Ion-exchanged water was added to the fused silica spheres to obtain a slurry concentration as shown in Table 2. 1% ammonia water was added to adjust the slurry concentration to - as shown in Table 2, and the mixture was stirred for 30 minutes using a sand mill, and then stirred using a liquid cyclone. Fine powder was classified and removed.

この処理物の比表面積を第2表に示す。Table 2 shows the specific surface area of this treated product.

なお、粒度分布の測定はレーザー回折式沈降法により、
また、比表面積の測定は窒素吸着法(BET法)により
行った。
The particle size distribution was measured by laser diffraction sedimentation method.
Further, the specific surface area was measured by a nitrogen adsorption method (BET method).

第2表  処理後の溶融シリカ球状体 以上により、スラリーの−1を6〜9の範囲に調整する
と得られる溶融シリカ球状体の比表面積が小さくなるこ
と、すなわち、微粉が分離されることが明らかである。
Table 2 Fused silica spheres after treatment From the above, it is clear that when -1 of the slurry is adjusted to a range of 6 to 9, the specific surface area of the resulting fused silica spheres becomes smaller, that is, fine powder is separated. It is.

(発明の効果〕 本発明によれば微粉の付着のない溶融シリカ球状体を得
ることができる。
(Effects of the Invention) According to the present invention, it is possible to obtain fused silica spheres free from adhesion of fine powder.

Claims (1)

【特許請求の範囲】[Claims] 1、粉末シリカを高温火炎と共に噴射して得られた微粉
付着の溶融シリカ球状体に、水を加えてスラリーとし、
スラリーのpHを6〜9に調整して攪拌を行ないながら
微粉を分離し、それを除去することを特徴とする溶融シ
リカ球状体の製造方法。
1. Water is added to the fused silica spheres with fine powder adhering to them, which is obtained by injecting powdered silica together with high-temperature flames, to form a slurry.
A method for producing fused silica spheres, which comprises adjusting the pH of a slurry to 6 to 9 and separating and removing fine powder while stirring.
JP60236367A 1985-10-24 1985-10-24 Production of fused silica spherule Pending JPS6296310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60236367A JPS6296310A (en) 1985-10-24 1985-10-24 Production of fused silica spherule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60236367A JPS6296310A (en) 1985-10-24 1985-10-24 Production of fused silica spherule

Publications (1)

Publication Number Publication Date
JPS6296310A true JPS6296310A (en) 1987-05-02

Family

ID=16999745

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60236367A Pending JPS6296310A (en) 1985-10-24 1985-10-24 Production of fused silica spherule

Country Status (1)

Country Link
JP (1) JPS6296310A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009072218A1 (en) * 2007-12-07 2009-06-11 Catalysts & Chemicals Industries Co., Ltd. Porous silica particle having surface smoothness, method for production of the porous silica particle, and cosmetic comprising the porous silica particle

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009072218A1 (en) * 2007-12-07 2009-06-11 Catalysts & Chemicals Industries Co., Ltd. Porous silica particle having surface smoothness, method for production of the porous silica particle, and cosmetic comprising the porous silica particle
JP2009137806A (en) * 2007-12-07 2009-06-25 Jgc Catalysts & Chemicals Ltd Porous silica particle having surface smoothness, manufacturing process of the porous silica particle, and cosmetic mixed with the porous silica particle
US9327258B2 (en) 2007-12-07 2016-05-03 Jgc Catalysts And Chemicals Ltd. Porous silica-based particles having smooth surface, method for production thereof and cosmetic comprising such particles

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