JPH07157308A - Method for producing synthetic quartz glass powder - Google Patents
Method for producing synthetic quartz glass powderInfo
- Publication number
- JPH07157308A JPH07157308A JP5306497A JP30649793A JPH07157308A JP H07157308 A JPH07157308 A JP H07157308A JP 5306497 A JP5306497 A JP 5306497A JP 30649793 A JP30649793 A JP 30649793A JP H07157308 A JPH07157308 A JP H07157308A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- quartz glass
- glass powder
- gel
- synthetic quartz
- 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
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 239000000843 powder Substances 0.000 title claims abstract description 49
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 7
- 239000000741 silica gel Substances 0.000 claims abstract description 15
- 229910002027 silica gel Inorganic materials 0.000 claims abstract description 15
- 238000010304 firing Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims description 10
- 239000011521 glass Substances 0.000 claims description 2
- 230000003301 hydrolyzing effect Effects 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 4
- 230000007062 hydrolysis Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 239000000499 gel Substances 0.000 description 18
- 235000012239 silicon dioxide Nutrition 0.000 description 9
- 239000010453 quartz Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000013078 crystal Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000004065 semiconductor Substances 0.000 description 4
- 238000003980 solgel method Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 125000003545 alkoxy group Chemical group 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- -1 etc. Chemical compound 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011240 wet gel Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C12/00—Powdered glass; Bead compositions
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/06—Glass compositions containing silica with more than 90% silica by weight, e.g. quartz
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C2201/00—Glass compositions
- C03C2201/02—Pure silica glass, e.g. pure fused quartz
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C2203/00—Production processes
- C03C2203/20—Wet processes, e.g. sol-gel process
- C03C2203/26—Wet processes, e.g. sol-gel process using alkoxides
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
(57)【要約】
【目的】 超高純度石英ガラス製品の原料として好適な
石英ガラス粉。
【構成】 テトラアルコキシシランの加水分解により得
たシリカゲルの粉末を焼成することによりご合成石英ガ
ラス粉を製造する際、焼成時に該シリカゲル粉末を流動
させながら焼成することを特徴とする合成石英ガラス粉
の製造方法。(57) [Summary] [Purpose] Quartz glass powder suitable as a raw material for ultra-high purity quartz glass products. [Composition] A synthetic quartz glass powder, characterized in that, when a synthetic silica glass powder is produced by firing a silica gel powder obtained by hydrolysis of tetraalkoxysilane, the silica gel powder is fired while flowing during the firing. Manufacturing method.
Description
【0001】[0001]
【産業上の利用分野】本発明は半導体製造分野、特に1
000℃以上の高温度域で使用される超高純度石英ガラ
ス製品の原料として好適な石英ガラス粉を提供するもの
である。FIELD OF THE INVENTION The present invention relates to the field of semiconductor manufacturing, in particular 1.
The present invention provides a quartz glass powder suitable as a raw material for an ultra-high purity quartz glass product used in a high temperature range of 000 ° C or higher.
【0002】[0002]
【従来の技術】従来、半導体単結晶製造用のルツボや治
具等は、天然石英を粉砕して得た天然石英粉を溶融して
製造されていたが、天然石英は良質のものであっても種
々の金属不純物を含んでおり、純度の面から十分満足し
得るものではなかった。特に、半導体産業の高性能化に
伴って要求される高純度単結晶には、金属不純物が混入
すると半導体の性能に悪影響を与えるので、金属不純物
等の混入が懸念されるようなルツボや治具等を使用する
ことは出来ない。この為、最近では、合成による高純度
な石英ガラス粉が必要になってきている。2. Description of the Related Art Conventionally, crucibles and jigs for manufacturing semiconductor single crystals have been manufactured by melting natural quartz powder obtained by crushing natural quartz, but natural quartz is of high quality. Also contains various metal impurities, and was not sufficiently satisfactory in terms of purity. In particular, in a high-purity single crystal that is required as the semiconductor industry becomes more sophisticated, if metal impurities are mixed, the performance of the semiconductor will be adversely affected. Cannot be used. For this reason, recently, high-purity silica glass powder synthesized has been required.
【0003】近年、純度的にすぐれたシリカ源として、
アルコキシシランを原料としたゾル・ゲル法によるシリ
カガラスが紹介されている。例えば、特開昭62−17
6928号公報には、アルコキシシランを酸とアルカリ
の存在下、加水分解してゲルを調整し、これを粉砕、乾
燥した後、焼成して石英ガラス粉を製造する方法が示さ
れている。In recent years, as a highly pure silica source,
Silica glass produced by sol-gel method using alkoxysilane as a raw material has been introduced. For example, JP-A-62-17
Japanese Patent No. 6928 discloses a method in which an alkoxysilane is hydrolyzed in the presence of an acid and an alkali to prepare a gel, which is crushed, dried, and fired to produce a quartz glass powder.
【0004】[0004]
【発明が解決しようとする課題】ゾル・ゲル法による合
成石英ガラス粉の製造では、原料としてアルコキシシラ
ンを用い、これを加水分解・縮重合させてウエットゲル
とし、更に副生したアルコールや水を乾燥除去してドラ
イゲルとする。ところが、アルコキシ基の100%が反
応してしまうわけではなく、一部がドライゲル中に結合
アルコキシ基として残留している。さらに、反応で副生
したアルコールも一部がドライゲル中に取り残されてい
る。実際、ドライゲル中のカーボン濃度を測定すると約
10,000〜15,000ppmである。In the production of synthetic quartz glass powder by the sol-gel method, alkoxysilane is used as a raw material, which is hydrolyzed and polycondensed to form a wet gel, and alcohol and water produced as by-products are further added. Dry and remove to obtain dry gel. However, 100% of the alkoxy groups do not react, and some remain as bonded alkoxy groups in the dry gel. Furthermore, some of the alcohol by-produced in the reaction is left behind in the dry gel. In fact, the carbon concentration in the dry gel is about 10,000 to 15,000 ppm.
【0005】このドライゲルを焼成すると大部分のカー
ボン分は燃焼除去されるが、一部が未燃カーボンとなっ
てガラス中に閉じこめられ黒色異物となることがある。
この黒色異物が合成石英粉の製品中に混入していると、
ルツボやインゴットに成形するために溶融した際、CO
やCO2 ガスとなって発泡の原因となる。このようにし
て得られた泡を含んだ石英ルツボや炉心管等では、高温
使用時の寸法安定性や、単結晶引き上げ時に泡が弾けて
液面揺動、結晶欠陥になる等の問題があった。When this dry gel is fired, most of the carbon content is burned and removed, but part of it becomes unburned carbon and may be trapped in the glass to become black foreign matter.
If this black foreign substance is mixed in the product of synthetic quartz powder,
When melted to form crucibles or ingots, CO
And becomes CO 2 gas and causes foaming. The quartz crucible and core tube containing bubbles obtained in this way have problems such as dimensional stability during high temperature use, bubbles popping when pulling a single crystal, and liquid level fluctuations and crystal defects. It was
【0006】[0006]
【課題を解決するための手段】発明者等は上記のような
不都合のない合成石英ガラス粉を得るため、鋭意研究を
重ねた結果、ゾル・ゲル法による合成石英ガラス粉の製
造において、乾燥シリカゲル粉末を焼成する工程におい
て、該シリカゲル粉末を流動させることにより、製品中
の黒色異物が少なく、引いては溶融成形時に泡の少ない
合成石英ガラス粉を得ることが出来ることを見出し、本
発明に到達した。Means for Solving the Problems The inventors of the present invention have conducted extensive studies in order to obtain synthetic quartz glass powder without the above-mentioned inconvenience, and as a result, in the production of synthetic quartz glass powder by the sol-gel method, dried silica gel In the step of firing the powder, it was found that by flowing the silica gel powder, it is possible to obtain a synthetic quartz glass powder with less black foreign matter in the product, and consequently less bubbles during melt molding, and arrived at the present invention. did.
【0007】以下、本発明につき、さらに詳細に説明す
る。本発明で対象となる合成石英ガラス粉は、アルコキ
シシランを加水分解して得られるシリカゲルを乾燥後、
焼成することにより得られる石英ガラス粉である。ゾル
ゲル法によるアルコキシシランの加水分解は、周知の方
法にしたがって、アルコキシシランと水を反応させるこ
とによって行なわれる。原料として用いられるアルコキ
シシランとしてはテトラメトキシシラン、テトラエトキ
シシラン等のC1 〜C4 の低級アルコキシシラン或いは
そのオリゴマーが好ましい。The present invention will be described in more detail below. The synthetic quartz glass powder targeted in the present invention is obtained by drying silica gel obtained by hydrolyzing alkoxysilane,
It is a quartz glass powder obtained by firing. Hydrolysis of alkoxysilane by the sol-gel method is performed by reacting alkoxysilane with water according to a known method. The alkoxysilane used as a raw material is preferably a C 1 -C 4 lower alkoxysilane such as tetramethoxysilane or tetraethoxysilane or an oligomer thereof.
【0008】水の使用量は通常、アルコキシシラン中の
アルコキシ基の1倍当量以上10倍当量以下から選択す
る。この際、必要に応じてアルコール類やエーテル類等
の有機溶媒を混合してもよい。アルコールとしてはメタ
ノール、エタノール、プロパノール、ブタノール等が、
エーテルとしてはアセトン等が挙げられる。また、触媒
として塩酸、酢酸のような酸やアンモニウムのようなア
ルカリを用いてもよい。当然のことながら、高純度の石
英ガラス粉を得るには、ここで使用する原料アルコキシ
シラン、水、溶媒等この反応系に導入される物質は、す
べて高純度であることが必要である。The amount of water used is usually selected from 1 to 10 equivalents of the alkoxy groups in the alkoxysilane. At this time, organic solvents such as alcohols and ethers may be mixed if necessary. As alcohol, methanol, ethanol, propanol, butanol, etc.,
Acetone etc. are mentioned as ether. Further, an acid such as hydrochloric acid or acetic acid or an alkali such as ammonium may be used as a catalyst. As a matter of course, in order to obtain a high-purity quartz glass powder, it is necessary that all the raw materials used here such as alkoxysilane, water, and solvent, which are introduced into this reaction system, have a high purity.
【0009】加水分解生成物をゲル化させるには、加熱
すれば直ちにゲルを得ることが出来るが、常温で放置し
ても数時間でゲル化するので、加温の程度を調節するこ
とによってゲル化時間を調節することが出来る。得られ
たゲルは細分化してから乾燥してもよいし、乾燥してか
ら細分化してもよい。乾燥シリカゲル粉末の粒径は、6
0〜900μm、好ましくは80〜800μmである。
ゲルの乾燥の程度については、H2 O含有量で通常、1
〜10重量%であり、通常、ゲルを真空中或いは不活性
ガス中で100〜200℃に加熱することにより行なわ
れる。In order to gel the hydrolysis product, the gel can be obtained immediately by heating, but even if it is left at room temperature, it will gel in a few hours. Therefore, by adjusting the degree of heating, the gel can be obtained. The aging time can be adjusted. The obtained gel may be subdivided and then dried, or may be dried and subdivided. The particle size of dry silica gel powder is 6
It is 0 to 900 μm, preferably 80 to 800 μm.
Regarding the degree of drying of the gel, the H 2 O content is usually 1
10 to 10% by weight, and it is usually carried out by heating the gel to 100 to 200 ° C. in vacuum or in an inert gas.
【0010】上記のようにして製造した乾燥シリカゲル
粉を、以下に述べる特定の焼成条件下で焼成する。すな
わち、空気雰囲気下乃至酸素濃度のより高い雰囲気下に
おいて、シリカゲル粉末を流動させながら、焼成を行な
うものである。この流動は、焼成の全期間行っても良い
が、以下に説明する要件を考慮して特定の温度領域のみ
を効果的に行っても良い。この様な温度領域としては、
ゲルが無孔化する1000℃以下、特に400〜800
℃の領域であり、且つこの領域で酸素温度を高めると本
発明の効果を向上させたり、焼成時間の短縮が図れる。
例えば、円筒型の石英容器にシリカゲル粉末を仕込み、
該円筒容器を回転させることにより、粉体層を流動させ
る方法がある。但し、粉体を流動させる方法としては、
特にこの方法に限定されるものではなく、例えば、ルツ
ボにシリカゲル粉末を仕込み、その下層部より、空気等
をバブリングさせる等の方法によっても行なうことが出
来る。通常、このシリカゲル粉末を静置した状態で焼成
を行なうと、粉体下層部まで、酸素の拡散が十分に行き
渡らず、カーボン含有物が完全に酸化されずに、未燃カ
ーボンとなって、黒色異物の発生原因となる。これに対
し、常に粉体層を流動させてやることにより、各シリカ
ゲル粒子は、十分に酸素と接触し、ひいては、黒色異物
の発生を大幅に押さえることが可能となった。ここで、
焼成時の、昇温速度としては、特に、ゲルの封孔前であ
る、800℃以下において、1000℃/Hr以下、好
ましくは、500℃/Hr以下としてやることが好まし
い。これよりも、急速に昇温を行なうと、カーボンが完
全に酸化される前に、ゲルが封孔し、黒色異物の発生を
押さえる効果が、あまり期待できない。また、途中、4
00〜800℃の範囲において、0.5〜5時間程度の
保持を行うのも効果的である。この場合、空気雰囲気で
は1.5〜5時間酸素高濃度下では0.5〜3時間が好
ましい。このようにして、最終的に、1000〜140
0℃まで焼成し、ゲルの無孔化を行い、合成シリカガラ
ス粉を得る。The dried silica gel powder produced as described above is fired under the specific firing conditions described below. That is, firing is performed while flowing the silica gel powder in an air atmosphere or an atmosphere having a higher oxygen concentration. This flow may be performed for the entire period of firing, or may be performed effectively only in a specific temperature region in consideration of the requirements described below. For such temperature range,
1000 ° C or less at which the gel becomes non-porous, especially 400 to 800
If the temperature is in the range of ° C and the oxygen temperature is raised in this range, the effect of the present invention can be improved and the firing time can be shortened.
For example, charge silica gel powder into a cylindrical quartz container,
There is a method of flowing the powder layer by rotating the cylindrical container. However, as a method of flowing the powder,
The method is not particularly limited to this method. For example, a method of charging silica gel powder into a crucible and bubbling air or the like from the lower layer portion thereof can be used. Normally, when this silica gel powder is calcined in a stationary state, oxygen is not sufficiently diffused to the lower layer of the powder, the carbon-containing material is not completely oxidized, and it becomes unburned carbon to give a black color. It may cause foreign matter. On the other hand, by constantly flowing the powder layer, each silica gel particle was brought into sufficient contact with oxygen, and it was possible to significantly suppress the generation of black foreign matter. here,
The temperature rising rate during firing is preferably 1000 ° C./Hr or less, and more preferably 500 ° C./Hr or less, particularly at 800 ° C. or less before sealing the gel. When the temperature is raised more rapidly than this, the effect of suppressing the generation of black foreign matter cannot be expected so much because the gel seals before the carbon is completely oxidized. Also, on the way, 4
It is also effective to hold the material in the range of 00 to 800 ° C. for about 0.5 to 5 hours. In this case, it is preferably 1.5 to 5 hours in an air atmosphere and 0.5 to 3 hours under a high oxygen concentration. Thus, finally, 1000-140
The mixture is baked to 0 ° C. to make the gel non-porous to obtain synthetic silica glass powder.
【0011】このようにして得られた石英ガラス粉は、
粉体の流動を行なわずに焼成した物と比べ、極めて黒色
異物の少ないものとなる。この、黒色異物の極めて少な
いシリカガラス粉末を溶融成形すると、非常に泡の少な
いインゴットやルツボを製造することが出来る。The quartz glass powder thus obtained is
Compared to the product obtained by firing without flowing the powder, the amount of black foreign matter is extremely small. When this silica glass powder containing very few black foreign matters is melt-molded, ingots and crucibles with very few bubbles can be produced.
【0012】[0012]
【実施例】以下、実施例によって、本発明を具体的に説
明するが、本発明は、その要旨を越えない限り、以下の
実施例に限定されるものではない。 実施例−1 撹拌槽に、テトラメトキシシランとこれに対して5倍当
量の水を仕込み、30℃の温度で1時間撹拌し、加水分
解反応によって均一なゾル溶液を得た。さらに、これを
塩化ビニル製のバットに移し、24時間放置して、ゲル
化させた。このゲルを、140℃の真空乾燥機を用いて
12時間乾燥を行なった後、100〜500μmの粒子
径に粒度調整を行なった。このようにして得られたシリ
カガラス粉末1.5kgを、ロータリーキルン型の電気
炉の、石英ガラス製内管に仕込んだ。この石英管の左側
から、空気を101/minで供給しながら、2rpm
で石英管を回転させ、200℃/Hrの昇温速度で12
00℃まで昇温し、この温度で10時間保持した。自然
冷却後、この合成石英ガラス粉末を取り出し、その中の
黒色異物の数を目視で調べたところ、8個であった。ま
た、この粉末を酸素−水素炎の加熱によるベルヌイ型溶
融装置を用いて溶融し、12mmφ×50mmのインゴ
ットを作製し、発泡状態を調べたところ、ごく小さな泡
が1個見られた。EXAMPLES The present invention will be described in detail below with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist. Example-1 Tetramethoxysilane and water in an amount 5 times equivalent thereto were charged in a stirring tank and stirred at a temperature of 30 ° C. for 1 hour to obtain a uniform sol solution by hydrolysis reaction. Further, this was transferred to a vinyl chloride vat and left for 24 hours for gelation. After drying this gel for 12 hours using a vacuum dryer at 140 ° C., the particle size was adjusted to a particle size of 100 to 500 μm. 1.5 kg of the silica glass powder thus obtained was charged into a quartz glass inner tube of a rotary kiln type electric furnace. 2 rpm while supplying air at 101 / min from the left side of this quartz tube
Rotate the quartz tube at 12 ° C at a heating rate of 200 ° C / Hr.
The temperature was raised to 00 ° C. and the temperature was maintained for 10 hours. After natural cooling, the synthetic quartz glass powder was taken out, and the number of black foreign matters therein was visually examined to find that it was eight. Further, this powder was melted using a Bernoulli type melting device by heating with an oxygen-hydrogen flame to prepare an ingot of 12 mmφ × 50 mm, and the foaming state was examined. As a result, one very small bubble was found.
【0013】実施例−2 実施例1において、焼成条件を、200℃/Hrで60
0℃まで昇温し、この温度で2時間保持した後、さらに
200℃/Hrで1200℃まで昇温し、この温度で1
0時間保持する事により行なった。そして、同様に得ら
れた合成石英ガラス粉末中の黒色異物の数を目視で調べ
たところ、1個であった。さらに、この粉末でベルヌイ
法により12mmφ×50mmのインゴットを作製した
ところ、泡は皆無であった。Example 2 In Example 1, the firing conditions were 200 ° C./hr and 60
After raising the temperature to 0 ° C. and holding at this temperature for 2 hours, the temperature was further raised to 1200 ° C. at 200 ° C./Hr and the
It was carried out by holding for 0 hour. Then, when the number of black foreign matters in the synthetic quartz glass powder obtained in the same manner was visually inspected, it was one. Furthermore, when a 12 mmφ × 50 mm ingot was produced from this powder by the Bernoulli method, no bubbles were found.
【0014】比較例−1 実施例1と同様の方法で乾燥シリカゲル粉末を作製し、
150mmφ×150mmHの石英ガラス製ルツボに
1.5kg仕込んだ。この時の、粉体層高は、120m
mであった。このルツボを、電気炉内にセットし、ルツ
ボ表面に空気を101/minで流しながら、200℃
/Hrで1200℃まで昇温し、この温度で10時間保
持した。自然冷却後、得られた合成石英ガラス粉末中の
黒色異物の数を目視で調べたところ、45個/kgであ
った。さらに、この粉末でベルヌイ法により、12mm
φ×50mmのインゴットを作製したところ、非常に多
くの泡(このうち0.5mmφ以上の大きな泡3個)が
見られた。Comparative Example-1 A dried silica gel powder was prepared in the same manner as in Example 1,
1.5 kg was charged into a 150 mmφ × 150 mmH quartz glass crucible. At this time, the powder bed height is 120 m
It was m. This crucible was set in an electric furnace, and air was flowed on the surface of the crucible at a rate of 101 / min at 200 ° C.
The temperature was raised to 1200 ° C. with / Hr, and the temperature was maintained for 10 hours. After natural cooling, the number of black foreign matters in the obtained synthetic quartz glass powder was visually inspected and found to be 45 / kg. Furthermore, by this Bernoulli method with this powder, 12 mm
When a φ × 50 mm ingot was produced, a very large number of bubbles (including 3 large bubbles of 0.5 mmφ or more) were observed.
【0015】[0015]
【発明の効果】本発明により黒色異物の少ない石英ガラ
ス粉を得ることができる。Industrial Applicability According to the present invention, it is possible to obtain a silica glass powder containing less black foreign matter.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 永井 浩昭 北九州市八幡西区黒崎城石1番1号 三菱 化成株式会社黒崎工場内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Hiroaki Nagai 1-1 Kurosaki Shiroishi, Hachimansai-ku, Kitakyushu City Mitsubishi Kasei Co., Ltd. Kurosaki Plant
Claims (2)
り得たシリカゲルの粉末を焼成することにより合成石英
ガラス粉を製造するにあたり、焼成時に、該シリカゲル
粉末を流動させながら焼成することを特徴とする合成石
英ガラス粉の製造方法。1. A synthetic quartz glass powder produced by hydrolyzing a tetraalkoxysilane, which is calcined while flowing the silica gel powder when the synthetic silica glass powder is produced. Glass powder manufacturing method.
いてシリカゲル粉末を流動させることを特徴とする請求
項1記載の製造方法。2. The method according to claim 1, wherein the silica gel powder is made to flow at 400 to 800 ° C. in the firing step.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5306497A JPH07157308A (en) | 1993-12-07 | 1993-12-07 | Method for producing synthetic quartz glass powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5306497A JPH07157308A (en) | 1993-12-07 | 1993-12-07 | Method for producing synthetic quartz glass powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH07157308A true JPH07157308A (en) | 1995-06-20 |
Family
ID=17957741
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5306497A Pending JPH07157308A (en) | 1993-12-07 | 1993-12-07 | Method for producing synthetic quartz glass powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07157308A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08301614A (en) * | 1995-04-28 | 1996-11-19 | Mitsubishi Chem Corp | Method for producing synthetic quartz powder and method for producing molded quartz glass |
| JP2001089169A (en) * | 1999-09-28 | 2001-04-03 | Shinetsu Quartz Prod Co Ltd | Method for producing synthetic quartz glass powder |
-
1993
- 1993-12-07 JP JP5306497A patent/JPH07157308A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08301614A (en) * | 1995-04-28 | 1996-11-19 | Mitsubishi Chem Corp | Method for producing synthetic quartz powder and method for producing molded quartz glass |
| JP2001089169A (en) * | 1999-09-28 | 2001-04-03 | Shinetsu Quartz Prod Co Ltd | Method for producing synthetic quartz glass powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH072513A (en) | Method for producing synthetic quartz glass powder | |
| EP0474158B1 (en) | Silica glass powder and a method for its production and a silica glass body product made thereof | |
| JPH10287416A (en) | Method for producing synthetic quartz powder | |
| JPH0826742A (en) | Synthetic quartz glass powder | |
| JP3832113B2 (en) | Aluminum-containing synthetic quartz glass powder, aluminum-containing quartz glass molded body, and methods for producing them | |
| JPH054827A (en) | Silica glass powder, method for producing the same, and silica glass molding using the same | |
| JP3617153B2 (en) | Method for producing synthetic quartz powder | |
| JP3318946B2 (en) | Powdery dry gel, silica glass powder, and method for producing silica glass melt molded article | |
| JP3724084B2 (en) | Method for producing synthetic quartz powder and quartz glass molded body | |
| JP3772453B2 (en) | Method for producing aluminum-containing synthetic quartz powder | |
| JP3735886B2 (en) | Method for producing synthetic quartz powder and method for producing quartz glass molded body | |
| JP3884783B2 (en) | Method for producing synthetic quartz powder | |
| JP3859303B2 (en) | Method for producing synthetic quartz glass powder and quartz glass molded body | |
| JP3847818B2 (en) | Method for producing synthetic quartz glass powder | |
| JPH11349340A (en) | Method for producing synthetic quartz glass powder and method for producing quartz glass compact | |
| JPH10101322A (en) | Silica gel, synthetic quartz glass powder, method for producing the same, and method for producing quartz glass compact | |
| JP3875735B2 (en) | Method for producing synthetic quartz powder | |
| JPH0826741A (en) | Method for producing synthetic quartz glass powder | |
| JP3847819B2 (en) | Method for producing synthetic quartz glass powder | |
| JPH10182140A (en) | Method for producing synthetic quartz glass powder and quartz glass compact | |
| JP4075193B2 (en) | Niobium-containing synthetic quartz glass powder, quartz glass molded body, and production method thereof | |
| JPH10203821A (en) | Method for producing synthetic quartz glass powder and quartz glass compact | |
| JPH06329406A (en) | Method for producing synthetic quartz glass powder | |
| JPH11349337A (en) | Method for producing synthetic quartz glass powder and method for producing quartz glass compact | |
| JP3806953B2 (en) | Method for producing synthetic quartz powder |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20040106 |
|
| A521 | Written amendment |
Effective date: 20040301 Free format text: JAPANESE INTERMEDIATE CODE: A523 |
|
| A131 | Notification of reasons for refusal |
Effective date: 20040330 Free format text: JAPANESE INTERMEDIATE CODE: A131 |
|
| A521 | Written amendment |
Effective date: 20040519 Free format text: JAPANESE INTERMEDIATE CODE: A523 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Effective date: 20040714 Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
| A61 | First payment of annual fees (during grant procedure) |
Effective date: 20040727 Free format text: JAPANESE INTERMEDIATE CODE: A61 |
|
| R150 | Certificate of patent (=grant) or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| R371 | Transfer withdrawn |
Free format text: JAPANESE INTERMEDIATE CODE: R371 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080813 Year of fee payment: 4 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080813 Year of fee payment: 4 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 5 Free format text: PAYMENT UNTIL: 20090813 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 5 Free format text: PAYMENT UNTIL: 20090813 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 6 Free format text: PAYMENT UNTIL: 20100813 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 7 Free format text: PAYMENT UNTIL: 20110813 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 7 Free format text: PAYMENT UNTIL: 20110813 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| R360 | Written notification for declining of transfer of rights |
Free format text: JAPANESE INTERMEDIATE CODE: R360 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| R360 | Written notification for declining of transfer of rights |
Free format text: JAPANESE INTERMEDIATE CODE: R360 |
|
| R371 | Transfer withdrawn |
Free format text: JAPANESE INTERMEDIATE CODE: R371 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| R360 | Written notification for declining of transfer of rights |
Free format text: JAPANESE INTERMEDIATE CODE: R360 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| R360 | Written notification for declining of transfer of rights |
Free format text: JAPANESE INTERMEDIATE CODE: R360 |
|
| R371 | Transfer withdrawn |
Free format text: JAPANESE INTERMEDIATE CODE: R371 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110813 Year of fee payment: 7 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 8 Free format text: PAYMENT UNTIL: 20120813 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130813 Year of fee payment: 9 |