JPS58176136A - Preparation of quartz glass powder - Google Patents

Preparation of quartz glass powder

Info

Publication number
JPS58176136A
JPS58176136A JP57060579A JP6057982A JPS58176136A JP S58176136 A JPS58176136 A JP S58176136A JP 57060579 A JP57060579 A JP 57060579A JP 6057982 A JP6057982 A JP 6057982A JP S58176136 A JPS58176136 A JP S58176136A
Authority
JP
Japan
Prior art keywords
raw material
quartz glass
water
glass powder
gel
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
JP57060579A
Other languages
Japanese (ja)
Inventor
Yasuo Kuroda
黒田 康雄
Hiroshi Ikeda
博 池田
Koichi Yamakawa
山川 幸一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Metal Corp
Original Assignee
Mitsubishi Metal Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Metal Corp filed Critical Mitsubishi Metal Corp
Priority to JP57060579A priority Critical patent/JPS58176136A/en
Publication of JPS58176136A publication Critical patent/JPS58176136A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL 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
    • C03C1/00Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
    • C03C1/006Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL 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
    • C03C13/00Fibre or filament compositions
    • C03C13/04Fibre optics, e.g. core and clad fibre compositions
    • C03C13/045Silica-containing oxide glass compositions
    • C03C13/046Multicomponent glass compositions
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL 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
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/06Glass compositions containing silica with more than 90% silica by weight, e.g. quartz

Abstract

PURPOSE:To obtain high-purity quartz glass powder in high yield, by adding water and an alcohol to a silicate to give a solution, dispersing or suspending the solution in a liquid having no compatibility with it to form powdery or granular gel, then calcining it. CONSTITUTION:100-300pts.vol. water and 0.25pts.vol. alcohol are added to 100pts.vol. silicate. The raw material solution is dispersed or suspended in a liquid such as hexane, xylene, etc., substantially having no compatibility with the raw material solution. Powdery or granular gel formed by the treatment is separated from the mother liquor, washed, dried, and calcined. By this method, high-purity quartz glass powder useful as a main raw material for optical fiber of multicomponent system is obtained in high yield without producing dust.

Description

【発明の詳細な説明】 本発明はダス)1発生させることなく、高純度の石英ガ
ラス粉末を高収率で製造する石英ガラス粉末の製省方法
4111する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for producing quartz glass powder with high yield and high purity without generating dust.

多成分系オプティカルファイバーのIMffiKは。IMffiK is a multi-component optical fiber.

石英カラス粉末を酸化ホウ素、炭酸ソーダ等のガラス形
成材料と混合し、浴−してホウ珪酸ガラス停の一体とし
、いわ−4る二直−ツボの底孔か・ら相朽的に扁い光屈
析卓t−mする組成のカラスが中心軸(コア)K位置す
るよう忙二重の組成のガラス−捧を同軸状に引出し、延
伸してオプティカルファイバーとするが、ガラス中に遭
移會属不純物が含まれる場合には光損失のもとくなるの
で高N度の原料が′1I11まれる。一方、シリコン、
砒化カリウム等の半4体単結晶の引上げ用石英ガラスル
ツボは便米天然氷lIi+粉をルツボ状に成形し、加熱
、半−化して製作さtlてきたが、天然水晶に#i各種
の不純書が含まれるため、良質の単結晶の要望が高まる
とともに該ルツボー高#B度品が望まれて贋る。
Quartz glass powder is mixed with glass-forming materials such as boron oxide and soda carbonate, and the mixture is heated in a bath to form a borosilicate glass stopper, which is gradually flattened from the bottom hole of the so-called four-sided acupuncture point. A glass fiber with a double composition is pulled out coaxially so that the glass with the composition to be measured is located on the central axis (core) K of the optical diffraction table, and stretched to form an optical fiber. If impurities are included, this will cause optical loss, so a raw material with a high N degree is used. On the other hand, silicon
Silica glass crucibles for pulling semi-quadramid single crystals such as potassium arsenide have been manufactured by molding natural ice lIi + powder into a crucible shape and heating it to semi-crystalize it, but natural crystal contains various impurities. As a result, the demand for high-quality single crystals increases, and high #B quality crucibles are desired and are often counterfeited.

さらに1石英カラス粉末よりホットプレス法に工って、
Q!−成形を鰻ることなく石英ガラスの成型体t−慢る
方法も開発されつつあり、その他大規漠喚横IgJ略の
パターン転写用ホトマスク基板としての石英ガラス板、
光学材料の製造原料として石英ガラス粉末は有望視され
るが1本発明による石英カラス粉末はこれらの目的にも
利用のoT能性が高い。
Furthermore, by using hot pressing method from 1 quartz glass powder,
Q! - A method for forming a quartz glass molded body without molding is also being developed, and a quartz glass plate as a photomask substrate for pattern transfer of large scale horizontal IgJ, etc.
Although quartz glass powder is considered to be promising as a raw material for producing optical materials, the quartz glass powder according to the present invention has high OT ability to be used for these purposes as well.

なお1本発明により製造される石英ガラス粉末は蒸舗岬
により容易Klf製される珪酸エチルを原料とすること
により、i1m純度のものが得られるが、特に原料WI
製を施さなくても石英ガラス粉末が得られることは明ら
かであり、また原料の珪酸エステルは半導体工業から多
量Kil生する四塩化珪素より酵導されるため、資源と
して限りのある天然氷島に代る汎用石英カラス原料とし
ても有用である。
Note that the silica glass powder produced according to the present invention can be obtained with i1m purity by using ethyl silicate, which is easily manufactured by Klf by Keiho Misaki, as a raw material, but especially when the raw material WI
It is clear that quartz glass powder can be obtained without any manufacturing, and since the raw material silicate ester is fermented from silicon tetrachloride, which is produced in large quantities in the semiconductor industry, it is possible to obtain quartz glass powder from natural ice islands, which are limited resources. It is also useful as an alternative raw material for general-purpose quartz glass.

従来1石英ガラス粉末としては、天然石英t−粉砕した
ものがあり、シリコン等亭導体単結晶の引上げ用ルツボ
の製造に使用されているが、天然石英にはもともと重金
属等あ不純物が含まれている辷、!!&砕工程でさらに
汚染がオぬかれな匹ため。
Conventional quartz glass powder is t-pulverized natural quartz, which is used to manufacture crucibles for pulling silicon single crystals, but natural quartz originally contains impurities such as heavy metals. Come on! ! & Because the contamination is further removed during the crushing process.

天然石英は上述したように、高純度1*する目的には不
適尚である。
As mentioned above, natural quartz is unsuitable for the purpose of achieving high purity 1*.

一方、高#1度の石英ガラス粉末の製法としてはたとえ
ば、酸水素炎による&!g塩化珪素の高温酸化により帰
られる高#1度合成カラス塊の粉砕も考えられるが、粉
砕に伴う汚染のため、純度を維持することが1離であり
、かつ粉砕により必然的に発生する倣粉末が粉砕ならび
にハンドリングの過根でダストとして飛散し、*m*生
上生麺問題る。
On the other hand, as a method for manufacturing quartz glass powder with a high #1 degree, for example, an oxyhydrogen flame is used. It is also possible to crush the high #1 synthetic glass mass produced by high-temperature oxidation of silicon chloride, but due to the contamination that accompanies the crushing, it is difficult to maintain purity, and the imitation that inevitably occurs due to crushing is considered. The powder is scattered as dust during crushing and handling, causing a problem with *m* raw raw noodles.

このIttc間龜の多い粉砕工種を要することなく高純
度の石英ガラス粉t4る方法として、本出劇人は、珪酸
エチルに*tla濁させることにより。
As a method for producing high-purity quartz glass powder without requiring a grinding process involving a large number of gaps, the author of the present invention proposes a method for producing quartz glass powder by clouding it with ethyl silicate.

粉粒状のゲルを生成させ、この粉粒状ゲルを焼成する方
法Yttp!iff出願(以下、先願といつ)している
が、この方法は収率が80チ楊夏であり、かつ主原料の
珪酸エチルの回収t4することが一点となっている。
A method for producing powdery gel and firing this powdery gel Yttp! IF has been filed (hereinafter referred to as "prior application"), but this method has a yield of 80 cm, and one point is that the main raw material, ethyl silicate, is recovered at t4.

本発明者らは先−発@iiを改良して石英ガラス粉収率
を高める方法t−提供すべく1種々検討した結果、珪酸
エステル100容緻と瞑珪鍍エステル100容量当り1
00乃至300容量の水とよりなる配合組成の均一な原
料溶液は多くの有機系溶媒等の液体と実質的に相溶性の
なhことに着目し、鋏原料溶液を咳原料溶液と実質的に
相溶性のない液体に該原料溶液の容量が該液体の容量よ
り過大でないように加えて激しく攪拌すると、咳原料浴
液が分散媒として作用する鋏液体中に細粒の液滴となっ
て分離、m濁し、この伏線を保持すると、粉粒体のゲル
が生成することを見出し1本発明Kffij!した。
The inventors of the present invention have conducted various studies to provide a method for increasing the yield of quartz glass powder by improving the original @ii.
Focusing on the fact that a raw material solution with a uniform composition consisting of 0.0 to 300 volumes of water is substantially miscible with many liquids such as organic solvents, the scissors raw material solution was substantially mixed with the cough raw material solution. When the raw material solution is added to an incompatible liquid so that the volume of the raw material solution is not larger than the volume of the liquid and stirred vigorously, the cough raw material bath liquid becomes fine droplets in the scissors liquid that acts as a dispersion medium and is separated. , and found that when this foreshadowing is maintained, a gel of the granular material is generated.1 The present invention Kffij! did.

すなわち1本発明の要旨とするところは、珪酸エステル
に該珪酸エステル100容量尚り100乃至300容量
の水を加えてなる原料溶tt、該原料#I?%[と実質
的に相溶性のな匹液体中に分散、懸濁させることKより
、粉粒状のゲルを生成させ。
That is, the gist of the present invention is to prepare a raw material solution tt prepared by adding 100 to 300 volumes of water to 100 volumes of the silicate ester, and the raw material #I? By dispersing or suspending a substance substantially miscible with K in a liquid, a powder-like gel is produced.

該粉粒状グルを分離し焼成することを特徴とする石英ガ
ラス粉末の製造方法、にある。
The present invention provides a method for producing quartz glass powder, which comprises separating and firing the granular powder.

本発明では上記水単昧の代りに水と水の0.25倍容量
を越えないアルコールとの混合物を珪酸エステルに加え
て原料溶液とすること4できる。このアルコールの使用
は、水単昧の場合には珪酸エステルと水の溶解速度が遅
く、原料溶液の調合に長時間を要するのに比べて、上記
原料溶液の調合を速かにするという効果がある。
In the present invention, a mixture of water and an alcohol not exceeding 0.25 times the volume of water can be added to the silicate ester to prepare the raw material solution4 instead of the water alone. The use of this alcohol has the effect of speeding up the preparation of the raw material solution, compared to the case where the silicate ester and water dissolve only in water, which would require a long time to prepare the raw material solution. be.

次K、本発明の各工程について詳述する。Next, each step of the present invention will be explained in detail.

tl)  原料溶液の調合工程 珪酸エステルに該珪酸エステル100容量当り100乃
至300容量の水を配合して原料溶ffILt−祠会す
る。この場合、壊酸エステル100容量当りの水の配合
量が100未満であると、に、記原料S液と多くの液体
との相溶度が増して収率の低下を来たし、逆圧水の配合
量がaoot越えると、生成する粉粒状ゲルが軟弱で互
に凝結しやすく粉体として得ることが1峻となる。この
工INにおいて、水単味の代りに、水と水の0.25倍
容量を越えないアルコールとの混合物t−珪酸エステル
に配合し調叶する場合は上述したように、原料溶液の調
合が促進されるうこのアルコールの配合量が水の0.2
5倍容量を越えると、多くの液体(分散媒)との相溶度
が増して収率の低下tきたす。
tl) Preparation process of raw material solution 100 to 300 volumes of water per 100 volumes of the silicate ester are blended to dissolve the raw material solution. In this case, if the amount of water mixed per 100 volumes of broken acid ester is less than 100, the compatibility of the raw material S liquid with many liquids will increase, resulting in a decrease in yield, and the If the blending amount exceeds aoot, the resulting powdery gel will be soft and easily coagulate with each other, making it difficult to obtain it as a powder. In this process, when mixing t-silicate ester, a mixture of water and alcohol not exceeding 0.25 times the volume of water, instead of using water alone, the raw material solution should be prepared as described above. The amount of alcohol that is promoted is 0.2 of that of water.
If the volume exceeds 5 times, the compatibility with many liquids (dispersion media) increases, resulting in a decrease in yield.

また、次工程のゲル化を促進するため、酸ないしアルカ
リを加えることは有効であり、装置の腐食ならびに廃液
、排ガスの対策を要するものの、4#l!、硝酸、硫@
  137酸、ギ酸、修酸、酢酸あるいはアンモニア等
を利用することもできる。
In addition, it is effective to add acid or alkali to promote gelation in the next step, and although measures must be taken to prevent equipment corrosion, waste liquid, and exhaust gas, 4#l! , nitric acid, sulfur @
137 acid, formic acid, oxalic acid, acetic acid, ammonia, etc. can also be used.

(2)粉粒状ゲルの生成工程 上記調合された原料溶液を咳原料溶液と実質的に相溶性
のない液体(分散1111t)Kmえて撤しく攪拌し、
該原料溶液が一粒の液滴となって該液体中に分散し懸濁
状態とする。
(2) Production process of powdery gel The raw material solution prepared above is thoroughly stirred after a liquid (dispersion 1111t) Km that is substantially incompatible with the cough raw material solution,
The raw material solution becomes a single droplet and is dispersed in the liquid to form a suspended state.

該液体としてtfi原料s液と実質的に相溶性がなけれ
ば%に限定されないが、11品のg2膳持の一点からは
ml!が容易で高1aK品が得やすいものが好ましく、
一方なるべく粘度が低(、比重が該原料溶液の比重(約
1)K近いものが咳原料溶液の液fI!4を鎖液体中に
十分に分散した懸濁状態を保持することを容易ならしめ
、かつ有利といえる。
As long as the liquid is not substantially compatible with the TFI raw material S liquid, it is not limited to %, but from one point of G2 serving of 11 items, ml! It is preferable that it is easy to obtain a high 1aK product.
On the other hand, a material with a low viscosity (with a specific gravity close to the specific gravity of the raw material solution (approximately 1) K) makes it easier to maintain the cough raw material solution fI!4 in a sufficiently dispersed state in the chain liquid. , and can be said to be advantageous.

さらに、#液体としては1、!J−エステルの加水分解
によりゲルが生成した後、残留する母液中には該珪酸エ
ステルの加水分解により副生するアルコールが混在する
ので、該液体の再利用と該アルコールの回収を考え、該
液体としては該嗣生アルコールを分離しやすいものが好
ましく、岡えば該アルコールと沸点差のなるべく大きい
ものが蒸溜分離がo]能となり有利となる。また、毒性
の強いもの、低沸点で取扱いの面倒なものは避けるべき
ことは勿論である。該液体の具体何としては次のような
液状化合物があるが、該液体はこれらの化汁物に限定さ
れるものではない。
Furthermore, #1 as a liquid! After a gel is generated by hydrolysis of J-ester, the remaining mother liquor contains alcohol, which is a by-product from the hydrolysis of the silicate ester. It is preferable to use an alcohol that can easily separate the successor alcohol, and it is advantageous to use an alcohol that has as large a difference in boiling point as possible from the alcohol because it can be separated by distillation. In addition, it goes without saying that highly toxic substances and substances with low boiling points that are difficult to handle should be avoided. Specific examples of the liquid include the following liquid compounds, but the liquid is not limited to these soups.

la)  へキサノ、キシレン等の脂肪族ないし芳香&
膨化水素。
la) Aliphatic or aromatic substances such as hexano, xylene, etc.
Expanding hydrogen.

lbJ  ヘキサノール、オクタツール等の高級アルコ
ール。
lbJ Higher alcohols such as hexanol and octatool.

LC)  ジエチルエーテル、アニソール等のエーテル
LC) Ethers such as diethyl ether and anisole.

(dl  バークロルエチレン、フロロベンゼン等のハ
ロゲン化炭化水嵩。
(dl Volume of halogenated hydrocarbons such as barchlorethylene and fluorobenzene.

le)  メチルイソブチ化ケトノ、シクロヘキサノン
等のカルボニル。
le) Carbonyl such as methylisobutylated ketono, cyclohexanone, etc.

(f)  ブチルフォスフェート等のエステル。(f) Ester such as butyl phosphate.

譲漱体の所4N菫としては、原料溶液と等量乃至は等量
以上が好ましく、紋液体の量が原料溶液の緻より過小に
なると、誼原料溶液の液滴が該液体中に分散した状態と
#iならず、逆に鋏液体のIli[f14が原、科溶液
中に分散するようkなり、粉粒状ゲルは生成しな匹。
It is preferable that the amount of 4N violet in the transfer body is equal to or more than the same amount as the raw material solution.If the amount of the 4N violet is less than the density of the raw material solution, droplets of the 4N violet solution may be dispersed in the liquid. On the contrary, the Ili[f14 in the scissors liquid became dispersed in the liquid solution, and no powdery gel was formed.

咳原料Saと咳液体の1合体を攪拌する方ff1Kd梼
に限定条件はなく、インペラー型の回転攪拌機、浮化重
合用浮化祷等が利用できる。
There are no limitations on the method of stirring the combination of the cough raw material Sa and the cough liquid, and an impeller-type rotary stirrer, a floater for floatation polymerization, etc. can be used.

室温で乃至はゲル生成速度を早めるため加熱しながら、
該原料#ll液と腋液体の混合体の攪拌を纏dすると1
分散した該原料溶液の液滴がゲル化し。
at room temperature or while heating to speed up gel formation.
Summarizing the stirring of the mixture of the raw material #1 liquid and the axillary liquid, 1 is obtained.
The dispersed droplets of the raw material solution gel.

粉粒状のゲルが生成する。該粉粒状ゲルの生成に要する
時間は実施例に示すように、咳原料靜液の配合組成、I
II会方#、、鍍混合の攪拌時の温度などに依存するが
、該原料溶液の液滴の性状を観察すること忙よっても知
ることができる。
A powdery gel is produced. The time required to produce the powdery gel depends on the composition of the cough material solution, I
Although it depends on the temperature during agitation during mixing, it can also be determined by observing the properties of the droplets of the raw material solution.

(3)  粉粒状ゲルの分離1鴨 、生成した該粉粒状グル上デカンテーション等により母
液から分離する。咳液体および該珪酸エステルより削生
したアルコールt−粉粒状ゲルより十分に除去すること
Fi後工楢の安全操作上好ましく。
(3) Separation of powdery gel 1. Separate the resulting powdery gel from the mother liquor by decantation or the like. It is preferable from the viewpoint of safe operation of the post-filtering process that the cough liquid and the alcohol t-powder-like gel removed from the silicate ester be sufficiently removed.

アルコール、次いで水、kLる洗浄が好適である。An alcohol followed by water wash is preferred.

(4)参稼状ゲルの乾燥1鶴 分離された#粒状ゲルを転轍する。この乾燥は必ずしも
不可欠な工程で#iなりが、乾燥により粉粒状ゲルが収
縮して嵩が大幅KaEするので1次の場或工橿の貢担に
@滅するために有効である。乾識a1度r1時に限定さ
れないが、250°Cまでに大−分の水が抜ける。
(4) Drying the granular gel.Turn over the separated #granular gel. This drying is an indispensable step, but it is effective for reducing the contribution of the primary process because the powdery gel shrinks due to drying and the bulk increases significantly. Although it is not limited to the dry temperature of 1 degree and 1 degree, a large amount of water is removed by 250 degrees Celsius.

(5)  粉粒状ゲルの焼成工種 乾燥した&粒状ゲル’i 1 、000°C付近の温度
で1@成し、ガラス化する。焼成時間は温度に依存する
が、概ね0.5乃至2時間であり、実施例を参考に決め
ることができる。
(5) Firing process of powdery gel The dried & granular gel 'i 1 is formed at a temperature around 1,000°C and vitrified. The firing time depends on the temperature, but is approximately 0.5 to 2 hours, and can be determined with reference to Examples.

なお、昇諷速イは時に限定されないが、乾燥不十分な粉
粒状ゲルを高速度で昇温すると、含有水の急激な揮発(
よって該粉粒状ゲルの粒子に割れや張れを生じ、S形1
粒度が変化するので、必要によっては低速外mを要する
〇 本@明は1以上のように、ダストを発生することな(、
高純度の石英カラス粉末を高収率で製造することを可能
ならしめる石英ガラス粉末の展進することを可能ならし
める石英ガラス粉末の製造法を提供するもので、多成分
ガラス系光伝送路。
Although the heating rate is not limited to certain times, heating a powdery gel that is insufficiently dried at a high rate will cause rapid volatilization of the water contained therein (
Therefore, cracks and tension occur in the particles of the powdery gel, resulting in S-shape 1.
Since the particle size changes, low speed external m is required depending on the need.
A multi-component glass optical transmission line is provided, which provides a method for producing quartz glass powder that enables the production of high-purity quartz glass powder at a high yield and enables the development of quartz glass powder.

半導体結晶引上げ用ルツボ等の製造上きわめて有用であ
る。
It is extremely useful in manufacturing crucibles for pulling semiconductor crystals, etc.

次に1本発明を実施例によってさらに具体的に説明する
が、本発明はその要旨を越えない限り以ドの実施例によ
って限定されるものでない。
Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples unless the gist thereof is exceeded.

実施例1 Alllilff製した珪酸メチル150ILlと4d
水]50dからなる混合浴液1g合して、謔溜梢製した
7クロヘキサン400−とと4KIJの六弗化テフロン
製ビーカーに入れ、テフロンコートしたインペラー型攪
拌欅で激しく攪拌し、液全体を一様に炎孔白色のS層状
態とした゛。操作は室温下で行った。
Example 1 Methyl silicate 150ILl and 4d manufactured by Allilff
1 g of a mixed bath solution consisting of 50 d of water] was put into a Teflon hexafluoride beaker made of 7 chlorohexane 400- and 4 KIJ, and stirred vigorously with a Teflon-coated impeller-type stirring cage to completely remove the entire liquid. The flame hole was uniformly in a white S-layer state. The operation was performed at room temperature.

約4時間後、核層濁液の′白色度が増したので、さらに
30分間攪拌t−継続して白色度に変化が感知されなく
なってから攪拌を止め、生成した粉粒状のゲルを母液よ
りデカンテーションによって分離し、蒸溜悄製したメタ
ノール各50mで4回、次いで蒸溜水50iuで3回洗
浄後、電気炉オープン内テ90°C−7l’204間乾
燥した。
After about 4 hours, the whiteness of the nuclear layer suspension increased, so the stirring was continued for another 30 minutes, and when no change in whiteness was detected, the stirring was stopped and the resulting powdery gel was removed from the mother liquor. It was separated by decantation, washed four times with 50 m of distilled methanol each time, and then three times with 50 iu of distilled water, and then dried in an open electric furnace at 90°C for 7 l'204.

乾燥後の粉粒状ゲルを電気炉で4時100°Cの割合で
昇温しl 、 050°Cで2時間焼成を何い、 56
.9?の焼成物t−漫だ、この焼成物の比重は2.20
であり1石英ガラスであることが確−された。また発光
分光分析を行なった結来、咳焼成物には不純債は積出さ
れず、+11i純度絡そあることが確められた。なお、
得られた粉粒体の粒子は径30乃至60μmの球状を呈
していた。収量56.9fは収率93噂に相当する。
After drying, the powdery gel was heated in an electric furnace at a rate of 100°C for 4 hours, and then baked at 050°C for 2 hours.
.. 9? The specific gravity of this fired product is 2.20.
1, and it was confirmed that it was quartz glass. In addition, emission spectroscopic analysis revealed no impurities in the cough scorch material, and it was confirmed that +11i purity was involved. In addition,
The particles of the obtained powder had a spherical shape with a diameter of 30 to 60 μm. The yield of 56.9f corresponds to a yield of 93 Rumor.

実権例2 4省悄装した珪酸エテル30d、漂溜水90−1蒸−稽
製したエタノールl1m、蒸溜水より再結4!?111
11した修鐵0,5?からなる混合溶液を祠脅し。
Practical example 2 30 d of silicic acid ether prepared in 4 parts, 1 ml of ethanol produced by distillation of 90-1 drifted water, and reconsolidated from distilled water 4! ? 111
11 Shutetsu 0.5? Threaten a mixed solution consisting of.

am拮aしたキシレン125dとともに四弗化テフロン
製三角フラスコ(容量300m)K入れ、コン    
 ′デンサー(MmRtl管)t−付けた上、65℃に
加熱しながら四弗化テフロンでコートしたマグ羊テイン
クスターラーで1.5時間激しく攪拌した。生成した粉
粒状のゲルを母液よりデカンテーシヨンによって分離し
、蒸溜N製したエタノール各30Mで4回1次いで蒸溜
水40+wjで2回洗浄後、電気オープン内で80°C
で15時間、250°Cで15時間乾燥した。スミで、
乾燥した粉粒状ゲルを電気炉内で毎時200’Cで1.
100’CK4mL、1時間焼成を行って7.9tの焼
成物1に得た。この焼成物の比l[は2.20で1石英
ガラスとなっており。
Pour a Teflon tetrafluoride Erlenmeyer flask (capacity 300 m) into a container with 125 d of xylene.
A denser (MmRtl tube) was attached, and the mixture was heated to 65°C and stirred vigorously for 1.5 hours using a mug stirrer coated with Teflon tetrafluoride. The resulting powdery gel was separated from the mother liquor by decantation, washed four times with 30M each of distilled N ethanol, and twice with distilled water 40+WJ, and then heated at 80°C in an electric open chamber.
for 15 hours and at 250°C for 15 hours. In Sumi,
The dried granular gel was heated in an electric furnace at 200'C/hour for 1.
4mL of 100'CK was fired for 1 hour to obtain 7.9t of fired product 1. The ratio l[ of this fired product is 2.20, which is 1 quartz glass.

収率は98慢である1発光分光分析を行ったM米。The yield is 98%. 1M rice subjected to emission spectroscopic analysis.

不純*は積出されず、高純度品であることが確められた
No impurity* was shipped, and it was confirmed that the product was of high purity.

実権例3 蒸溜+11111iした珪酸(正)プロピル20d、急
溜水50d、メタノール10−および0.INアンモニ
ア水0.1dからなる混合ml[を調合し、蒸舖稽製し
たイソオクタン120M、譲all楕製したテトラクロ
ルエチレン40317とともに六弗化テフロン糾三l向
フラスコ(容量300m)K入れ、室温くてマグ不テイ
ツクスターラーで2時間激しく攪拌した。
Practical Example 3 20 d of distilled +11111 (normal) propyl silicate, 50 d of distilled water, 10 methanol and 0. Prepare a mixture consisting of 0.1 d of IN ammonia water, and place it in a flask (capacity 300 m) containing Teflon hexafluoride with 120 M of isooctane prepared by steaming, and tetrachloroethylene 40317 prepared by distillation in a 3-liter flask (capacity 300 m) at room temperature. The mixture was stirred vigorously for 2 hours using a stainless steel stirrer.

生成した粉粒状ゲルを母液よりデカンチー7ヨンにより
分−り、J[M裏したエタノール各30dで4回1次い
で4盾水30111で2回洗浄後、電気オーブン内で8
0°Cで15時間、150°Cで8時間乾燥した。乾燥
した咳粉粒状ゲルを電気炉内で毎q100°Cの割合で
昇温し1,200°Cで30分閾椀成を行い3.6fP
の@成切1に得たうこの禰成+Wjの比重は2.20で
あり1発光分光分析により一〇不純物は積出されず、該
焼成物は高純(石英ガラス粉であることが確められた。
The resulting powdery gel was separated from the mother liquor by decanting, washed 4 times with 30 ml of ethanol and then twice with 30 111 ml of water, and then heated in an electric oven for 8 ml.
It was dried at 0°C for 15 hours and at 150°C for 8 hours. Dry cough powder granular gel was heated in an electric furnace at a rate of 100°C per qq and heated to 1,200°C for 30 minutes to form a threshold at 3.6 fP.
The specific gravity of the corn nemes + Wj obtained in @Narikiri 1 was 2.20, and 10 impurities were not detected by emission spectroscopic analysis, and the fired product was confirmed to be of high purity (it was confirmed that it was quartz glass powder). I was caught.

なj+5゜績児成吻の収1i3.6)は収率97嘩に相
当する。
A yield of +5° (1i3.6) corresponds to a yield of 97.

実施例4〜12 珪酸メチル100ajと第1表に示す容量の頑溜・にと
り蔦らなる混合溶液乃至は珪酸メチル100auと41
責に不す容量の蒸−水と各緻のメタノールとからノよる
混合Ia液を、同じく第1表に革す各分故森とともにス
テンレス製ビーカー(容量IJ)K入れ、アルミニウム
箔で覆って、40°CKI)I;J熱しl【から、四弗
化テフロンでコートしたマグネテイノクスターラーで2
.5時間激しく攪拌した。生成したゲルは実施例2の場
合と同様の処理を梱し−C比重2.20の石英ガラス粉
末を第1表に示す収率で得ることができた。
Examples 4 to 12 A mixed solution consisting of 100 aj of methyl silicate and 100 au of methyl silicate and 41
Put a mixture of Ia solution made from a reasonable amount of steam water and various amounts of methanol into a stainless steel beaker (capacity IJ), and cover it with aluminum foil, along with the various fractions shown in Table 1. , 40° CKI) I;
.. Stir vigorously for 5 hours. The produced gel was subjected to the same treatment as in Example 2, and quartz glass powder with a -C specific gravity of 2.20 could be obtained at the yield shown in Table 1.

第1表 比較ガニ〜4 、畦酸メチル10011jと第2浚に示す容量の4膚水
とよりなる混合′MfaL乃至は埴酸メチル100dと
嬉2表にボす合量のM溜水と容量のメタノールとよりな
る混合浴/fLf:、同じく第2表に示す皺のドデカ7
とともにステンレス製ビーカー(容量1りに入れ、実施
例3〜12の場合と同様に処理した。
Table 1 Comparison Gani ~ 4, a mixture consisting of 10011j of methyl borate and 100d of methyl borate and the volume of water shown in Table 2. A mixed bath consisting of methanol/fLf:, Wrinkled Dodeca 7 also shown in Table 2
The mixture was placed in a stainless steel beaker (capacity 1) and treated in the same manner as in Examples 3 to 12.

結果Vi第2表に示すように、蒸溜水の添加量が珪酸メ
チル100容量当り100容量より少ない場合ならびに
メタノール添加量が該頑溜水の添加量の0.25倍を越
える場合には、粉粒状のゲルは生成し、焼成によって石
英ガラス粉は得られるものの、その収4は著しく低いた
め、実用的ではなく、また無舗水の添加量が珪酸メチル
100容量当り300dlを越える場合には、粉粒状ゲ
ルの凝集体と考えられる粗大な塊りが生成するようにな
り、粉砕王様なくては石英ガラス粉は得られなかった。
As shown in Table 2 of Results Vi, when the amount of distilled water added is less than 100 volumes per 100 volumes of methyl silicate, and when the amount of methanol added exceeds 0.25 times the amount of distilled water, powder Although granular gel is produced and silica glass powder can be obtained by firing, the yield is extremely low, making it impractical, and if the amount of unsealed water exceeds 300 dl per 100 volumes of methyl silicate, Coarse lumps, which are considered to be aggregates of powdery gel, began to form, and quartz glass powder could not be obtained without crushing.

第2表Table 2

Claims (1)

【特許請求の範囲】 (l゛)珪酸エステルに該Ml鹸エステル100谷歇当
り100容量乃至300容量の水を加えてなる原料溶液
を、該原料溶液と実質的に相溶性のない液体中に分散、
#I!IHaさせることKより、粉粒状のゲルを生成さ
せ、#粉粒状ゲルを分離し濁成することt特徴とする石
英ガラス粉末の製造方法。 (2)  珪酸エステルに咳M#エステルIQQ谷緻尚
り100乃至300容量の水と皺水の0.25倍容量を
越えないアルコールとを加えてなる原料mgt、該原料
溶液と実質的tcse性のない液体中に分散、W4/l
llさせることにより、粉粒状のゲルを生成させ。 該粉粒状ゲルを分離しI@成すること1特徴とする石英
カラス粉末の製造方法。
[Claims] (1) A raw material solution prepared by adding 100 to 300 volumes of water per 100 volumes of the Ml sapon ester to a silicate ester is poured into a liquid that is substantially incompatible with the raw material solution. distributed,
#I! A method for producing quartz glass powder, characterized in that a powder-like gel is produced by IHa, and the powder-like gel is separated and turbidized. (2) Raw material mgt obtained by adding 100 to 300 volumes of water and alcohol not exceeding 0.25 times the volume of wrinkles water to silicate ester, and the raw material solution and substantial TCSE property. Dispersed in liquid without water, W4/l
ll to produce a powdery gel. A method for producing quartz glass powder, characterized in that the granular gel is separated and formed.
JP57060579A 1982-04-12 1982-04-12 Preparation of quartz glass powder Pending JPS58176136A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57060579A JPS58176136A (en) 1982-04-12 1982-04-12 Preparation of quartz glass powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57060579A JPS58176136A (en) 1982-04-12 1982-04-12 Preparation of quartz glass powder

Publications (1)

Publication Number Publication Date
JPS58176136A true JPS58176136A (en) 1983-10-15

Family

ID=13146293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57060579A Pending JPS58176136A (en) 1982-04-12 1982-04-12 Preparation of quartz glass powder

Country Status (1)

Country Link
JP (1) JPS58176136A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63291807A (en) * 1987-05-22 1988-11-29 Tonen Sekiyukagaku Kk Production of high-purity spherical silica
CN1300026C (en) * 2004-10-12 2007-02-14 西北有色金属研究院 Method for synthesizing high pure superfine biological glass powder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63291807A (en) * 1987-05-22 1988-11-29 Tonen Sekiyukagaku Kk Production of high-purity spherical silica
CN1300026C (en) * 2004-10-12 2007-02-14 西北有色金属研究院 Method for synthesizing high pure superfine biological glass powder

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