JPS6035295B2 - Silica glass manufacturing method - Google Patents

Silica glass manufacturing method

Info

Publication number
JPS6035295B2
JPS6035295B2 JP17446382A JP17446382A JPS6035295B2 JP S6035295 B2 JPS6035295 B2 JP S6035295B2 JP 17446382 A JP17446382 A JP 17446382A JP 17446382 A JP17446382 A JP 17446382A JP S6035295 B2 JPS6035295 B2 JP S6035295B2
Authority
JP
Japan
Prior art keywords
silica glass
alkoxyl
water
silicon
reaction
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
Application number
JP17446382A
Other languages
Japanese (ja)
Other versions
JPS5964542A (en
Inventor
昭一 須藤
裕之 須田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NTT Inc
Original Assignee
Nippon Telegraph and Telephone 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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP17446382A priority Critical patent/JPS6035295B2/en
Publication of JPS5964542A publication Critical patent/JPS5964542A/en
Publication of JPS6035295B2 publication Critical patent/JPS6035295B2/en
Expired 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
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/12Other methods of shaping glass by liquid-phase reaction processes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)
  • Glass Compositions (AREA)
  • Silicon Compounds (AREA)

Description

【発明の詳細な説明】 本発明はシリカガラスの製造方法に関する。[Detailed description of the invention] The present invention relates to a method for manufacturing silica glass.

Si(CH30)4等のアルコキシルシリコンを原料と
してシリカガラスを製造する場合、従来、CH30H‘
こよって希釈されたSi(CH30)4溶液に、競拝し
ながら、直接、NH40日を含んだ水を加えて固化(ゲ
ル化)させ、さらに乾燥、競結を経て、シリカガラス体
が得られていた。しかしながらこの従来の方法では、C
H30日によって希釈されたSj(CH30)4溶液に
、反応触媒であるNH40日を含んだ水を直接加えるの
で、該添加水中のN比OHの濃度が高すぎると、Sj(
CH30)4の加水分解反応が速すぎ、白色沈澱を生じ
て、固化(ゲル化)しない一方、該添加水中のN凡○日
濃度が低すぎると、加水分解反応が進行せず、ゲル化が
得られないという欠点があった。
When manufacturing silica glass using alkoxyl silicon such as Si(CH30)4 as a raw material, conventionally CH30H'
Thus, water containing NH40 was directly added to the diluted Si(CH30)4 solution, solidifying (gelling), and then drying and consolidating to obtain a silica glass body. was. However, in this conventional method, C
Since water containing NH40, which is a reaction catalyst, is directly added to the Sj(CH30)4 solution diluted by H30, if the concentration of N ratio OH in the added water is too high, Sj(
The hydrolysis reaction of CH30)4 is too fast, producing a white precipitate and not solidifying (gelling). On the other hand, if the concentration of N in the added water is too low, the hydrolysis reaction does not proceed and gelation occurs. The drawback was that it was not available.

すなわちアルコキシルシリコンにNH,OHを含んだ水
を直接加え、加水分解して、均一なゲル体を得るのは極
めて難しく、結果として良質なシリカガラスが得られな
いという欠点があった。本発明はこれらの欠点を除去す
るため、原料とするアルコキシルシリコンにあらかじめ
水を適量加えて混合した後、この混合溶液を反応触媒で
あるアンモニアを含むガス体に爆らし、固化(ゲル化)
せしめるものであり、その目的は、均一な加水分解反応
を実現して、均一なゲル体を得る手法を提供することに
よって、良質なシリカガラスの製造を可能にすることに
ある。
That is, it is extremely difficult to directly add water containing NH and OH to alkoxyl silicon and hydrolyze it to obtain a uniform gel body, resulting in a drawback that good quality silica glass cannot be obtained. In order to eliminate these drawbacks, the present invention involves adding an appropriate amount of water to alkoxyl silicon as a raw material, mixing it, and then exploding this mixed solution into a gaseous body containing ammonia, which is a reaction catalyst, to solidify (gel)
The purpose is to realize a uniform hydrolysis reaction and provide a method for obtaining a uniform gel body, thereby making it possible to manufacture high-quality silica glass.

第1図は、本発明の一実施例図であって、1は反応容器
、2はアルコキシルシリコン、アルコールおよび水の混
合液、3は発泡管、4は配管、5はサチュレータ、6は
アンモニア水である。
FIG. 1 is a diagram showing an embodiment of the present invention, in which 1 is a reaction vessel, 2 is a mixture of alkoxyl silicone, alcohol, and water, 3 is a foaming tube, 4 is piping, 5 is a saturator, and 6 is aqueous ammonia. It is.

第1図の実施例では、反応容器1内に入れたアルコキシ
ルシリコン、アルコールおよび水の混合液2を、サチュ
レ」夕5からArガスによって輸送される反応促進剤で
あるNH,0Hを含むアンモニア水の蒸気に、一定時時
間曝らした後、発泡管3を取り出し、該混合液2を固化
させるものである。今、前記実施例において、混合液2
として、Si(CH30)4,CH30日および日20
を1:2:3の体積比で含む溶液を10夕、またアンモ
ニア水6として5%NH40日液を使用した場合、30
oCの温度下において、毎分00そのArガスによって
輪騒されたアンモニアを含むガスに、1分間該混合液を
曝らすことによって均質なゲル体が得られた。この際、
ゲル化させるための薮触時間(曝らす時間)は、アンモ
ニア水中のNH40日濃度、反応温度、混合液中のSi
(CH30)4の割合に依存し、アンモニア水中のNH
40日濃度が高いほど、また反応温度が高いほど、さら
に混合液中のSi(CH30)4の割合が多いほど、ゲ
ル化のための接触時間は短くなる。なお混合液中のSj
(CH80)4の割合が一定値以下となると、N凡○日
濃度を高めても、また反応温度を高めても、ゲル化反応
は生じず、ゲル体は得られない。
In the embodiment shown in FIG. 1, a mixture 2 of alkoxyl silicon, alcohol and water placed in a reaction vessel 1 is mixed with ammonia water containing NH and 0H as reaction accelerators, which is transported from a saturator 5 by Ar gas. After being exposed to the steam for a certain period of time, the foaming tube 3 is taken out and the mixed liquid 2 is solidified. Now, in the above example, mixed liquid 2
As, Si(CH30)4, CH30 day and day 20
When a solution containing 1:2:3 volume ratio was used for 10 days, and a 5% NH solution was used as ammonia water 6 for 40 days, 30 days
A homogeneous gel body was obtained by exposing the mixed solution for 1 minute to a gas containing ammonia which was stirred by Ar gas at 0C/min. On this occasion,
The contact time (exposure time) for gelation depends on the 40-day concentration of NH in the ammonia water, the reaction temperature, and the Si in the mixture.
Depending on the proportion of (CH30)4, NH in ammonia water
The higher the 40-day concentration, the higher the reaction temperature, and the greater the proportion of Si(CH30)4 in the mixture, the shorter the contact time for gelation. In addition, Sj in the mixed liquid
When the ratio of (CH80)4 is below a certain value, no gelation reaction occurs and no gel body is obtained even if the concentration is increased or the reaction temperature is increased.

第2図は混合液のゲル化領域を示した図である。FIG. 2 is a diagram showing the gelation region of the mixed liquid.

縦軸は、日20とSi(CH30)4の割合割合(体積
比)を、機軸は、接触させるアンモニア水中のN凡○日
濃度(モル%)を示している。第2図からわかるように
、混合液中のSi(CH30)4割合が高い場合、接触
アンモニア水中のN比OH濃度が低くても容易にゲル化
するが、水の混合割合を大きくすると、ゲル化し1こく
くなり、第2図の曲線以上の領域条件ではゲル体は得ら
れなかった。以上のようにして得られた均質なゲル体を
乾燥した後、1400〜1500ooの温度で焼成する
ことによって良質な透明シリカガラス体が得られた。ま
た本発明で、アルコキシルシリコンに、他の金属アルキ
ル化合物、たとえばアルコキシルゲンマニウム、アルコ
キシルァルミニゥム、等を一定割合で混合した原料溶液
を使用した場合にも、前記と同様の操作によってゲル体
を得ることが可能であり、さらに該ゲル体を乾燥、競結
すると、ドープトシリカガラス体が得られる。以上説明
したように、本発明のシリカガラスの製造方法によって
、アルコキシルシリコンを原料として、容易に均質なゲ
ル体が得られ、さらにこのゲル体から良質なシリカガラ
ス体が得られる。
The vertical axis shows the proportion (volume ratio) of Si(CH30)4 and Si(CH30)4, and the axis shows the N concentration (mol %) in the ammonia water with which they are brought into contact. As can be seen from Figure 2, when the Si(CH30)4 ratio in the mixed solution is high, gelation occurs easily even if the N ratio OH concentration in the contact ammonia water is low, but when the mixing ratio of water is increased, gelation occurs. The gel body was not obtained under the condition of the area exceeding the curve shown in FIG. 2. After drying the homogeneous gel body obtained as described above, a high quality transparent silica glass body was obtained by firing at a temperature of 1400 to 1500 oo. In addition, in the present invention, when using a raw material solution in which alkoxyl silicone is mixed with other metal alkyl compounds such as alkoxyl germanium, alkoxyl aluminum, etc. at a certain ratio, the gel can be gelled by the same operation as described above. A doped silica glass body can be obtained by drying and coalescing the gel body. As explained above, according to the method for producing silica glass of the present invention, a homogeneous gel body can be easily obtained using alkoxyl silicon as a raw material, and a high-quality silica glass body can also be obtained from this gel body.

またこの良質なシリカガラス体およびドープトシリカガ
ラス体を素材として、高品質な光フアイバが得られる。
しかも本発明では、第1図に示した反応容器を大型化し
、大量のシリカガラス体を−度に製造することは容易で
あり、本発明の実施によって安価な光ファィバを提供で
きる利点がある。
Furthermore, high-quality optical fibers can be obtained using the high-quality silica glass body and doped silica glass body as raw materials.
Moreover, according to the present invention, it is easy to increase the size of the reaction vessel shown in FIG. 1 and manufacture a large amount of silica glass bodies at a time, and the present invention has the advantage of being able to provide inexpensive optical fibers.

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

第1図は本発明の一実施例図、第2図は混合液のゲル化
領域を示す図である。 1……反応容器、2……アルコキシルシリコン、アルコ
ールおよび水の混合液、3……発泡管、4・・・・・・
配管、5・・・・・・サチュレー夕、6・・・・・・ア
ンモニア水。 第1図 第2図
FIG. 1 is a diagram showing an embodiment of the present invention, and FIG. 2 is a diagram showing a gelation region of a mixed liquid. DESCRIPTION OF SYMBOLS 1... Reaction container, 2... Mixed liquid of alkoxyl silicone, alcohol, and water, 3... Foaming tube, 4...
Piping, 5...Saturation evening, 6...Ammonia water. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】 1 アルコキシルシリコンを原料としてシリカガラスを
製造するに際して、該アルコキシルシリコンをあらかじ
め水と混合した後に、この混合溶液をアンモニアをを含
むガス体に曝し、固化せしめ、さらに乾燥、焼成してシ
リカガラス体を得ることを特徴とするシリカガラスの製
造方法。 2 特許請求の範囲第1項記載のシリカガラスの製造方
法において、該アルコキシルシリコン原料中に、他の金
属アルコキシル化合物を含むことを特徴とするシリカガ
ラスの製造方法。
[Claims] 1. When producing silica glass using alkoxyl silicon as a raw material, the alkoxyl silicon is mixed with water in advance, and then this mixed solution is exposed to a gas containing ammonia to solidify, and then dried and fired. A method for producing silica glass, the method comprising: obtaining a silica glass body. 2. The method for producing silica glass according to claim 1, wherein the alkoxyl silicon raw material contains another metal alkoxyl compound.
JP17446382A 1982-10-06 1982-10-06 Silica glass manufacturing method Expired JPS6035295B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17446382A JPS6035295B2 (en) 1982-10-06 1982-10-06 Silica glass manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17446382A JPS6035295B2 (en) 1982-10-06 1982-10-06 Silica glass manufacturing method

Publications (2)

Publication Number Publication Date
JPS5964542A JPS5964542A (en) 1984-04-12
JPS6035295B2 true JPS6035295B2 (en) 1985-08-14

Family

ID=15978921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17446382A Expired JPS6035295B2 (en) 1982-10-06 1982-10-06 Silica glass manufacturing method

Country Status (1)

Country Link
JP (1) JPS6035295B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6287409A (en) * 1985-09-09 1987-04-21 Tama Kagaku Kogyo Kk Production of synthetic silica

Also Published As

Publication number Publication date
JPS5964542A (en) 1984-04-12

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