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JPH0466811B2 - - Google Patents
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JPH0466811B2 - - Google Patents

Info

Publication number
JPH0466811B2
JPH0466811B2 JP58132758A JP13275883A JPH0466811B2 JP H0466811 B2 JPH0466811 B2 JP H0466811B2 JP 58132758 A JP58132758 A JP 58132758A JP 13275883 A JP13275883 A JP 13275883A JP H0466811 B2 JPH0466811 B2 JP H0466811B2
Authority
JP
Japan
Prior art keywords
gel
glass
aqueous solution
gelling
producing
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
JP58132758A
Other languages
Japanese (ja)
Other versions
JPS6027611A (en
Inventor
Kenzo Susa
Iwao Matsuyama
Makoto Sato
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.)
Hitachi Cable Ltd
Hitachi Ltd
Original Assignee
Hitachi Cable Ltd
Hitachi 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 Hitachi Cable Ltd, Hitachi Ltd filed Critical Hitachi Cable Ltd
Priority to JP13275883A priority Critical patent/JPS6027611A/en
Publication of JPS6027611A publication Critical patent/JPS6027611A/en
Publication of JPH0466811B2 publication Critical patent/JPH0466811B2/ja
Granted 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

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)
  • Glass Melting And Manufacturing (AREA)
  • Colloid Chemistry (AREA)
  • Silicon Compounds (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はゾル・ゲル法によるガラス製造方法に
係り、特に、添加形シリカガラスの製造に適した
ゲルの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a method for producing glass by a sol-gel method, and particularly to a method for producing a gel suitable for producing additive-type silica glass.

〔発明の背景〕[Background of the invention]

従来、ゾル・ゲル法でガラス体を作成する場
合、第1図に示すとおり金属アルコキシドを水で
加水分解してゲルを作成し、ついでゲルを乾燥
し、さらに昇温焼結する。この場合、加水分解工
程では酸性、中性、アルカリ性のいずれを使用し
ても、ゲル作成が可能であるが、大形の透明ガラ
ス体を得ようとする場合はアルカリ性の水(例え
ばアンモニア水)で加水分解することが必須とな
つていた。その理由は、酸性や中性の条件で加水
分解を行なうと、細孔の小さく、かつゲルのかさ
密度が大きくなり、焼結過程で、ゲル細孔に残留
する吸着物(有機物、H2Oなど)による発泡現
象が生じるためである。これに比較して、アルカ
リ性の条件で加水分解する場合は、比較的細孔の
大きいかさ密度の低いゲルが作成でき、透明ガラ
ス化に際して、吸着ガスがスムーズに放出され発
泡などの不都合が生じにくいからである。
Conventionally, when producing a glass body by the sol-gel method, as shown in FIG. 1, a metal alkoxide is hydrolyzed with water to produce a gel, then the gel is dried, and then sintered at an elevated temperature. In this case, it is possible to create a gel by using acidic, neutral, or alkaline water in the hydrolysis process, but if you are trying to obtain a large transparent glass body, use alkaline water (for example, aqueous ammonia). It has become essential to hydrolyze it. The reason for this is that when hydrolysis is carried out under acidic or neutral conditions, the pores become smaller and the bulk density of the gel becomes larger. This is because a foaming phenomenon occurs due to (e.g.). In comparison, when hydrolysis is carried out under alkaline conditions, a gel with relatively large pores and low bulk density can be created, and during transparent vitrification, adsorbed gas is smoothly released and problems such as foaming are less likely to occur. It is from.

しかしながら、複数の成分から成るガラス体を
作成する場合、アルカリ性の条件で加水分解する
としばしば組成的に不均質のゲルが生成し、これ
を焼結したガラス体は不均質なものしか得られな
いという欠点があつた。
However, when creating a glass body consisting of multiple components, hydrolysis under alkaline conditions often produces a compositionally heterogeneous gel, and sintering this gel only yields a heterogeneous glass body. There were flaws.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、上記の欠点をなくした均質な
添加形透明ガラス体を製造するのに好適な均質ゲ
ルを製造する方法を提供することにある。
An object of the present invention is to provide a method for producing a homogeneous gel suitable for producing a homogeneous additive-type transparent glass body that eliminates the above-mentioned drawbacks.

〔発明の概要〕[Summary of the invention]

本発明の方法によれば、シリコンアルコキシド
または他の金属アルコキシドを含有するシリコン
アルコキシドを水または金属イオンを含有する水
溶液で加水分解し、ゲル化して乾燥せしめて成る
添加形シリカゲルの製造方法において、中性もし
くは酸性条件で加水分解せしめた後、アルカリ性
の条件でゲル化させることにより、細孔の大きい
均質度の高い添加形シリカゲルが製造できる。
According to the method of the present invention, in the method for producing additive silica gel, in which silicon alkoxide or silicon alkoxide containing other metal alkoxides is hydrolyzed with water or an aqueous solution containing metal ions, gelled and dried, Additive silica gel with large pores and high homogeneity can be produced by hydrolyzing it under acidic or acidic conditions and then gelling it under alkaline conditions.

〔発明の実施例〕[Embodiments of the invention]

以下実施例により詳述する。 This will be explained in detail below using examples.

実施例 第2図に示すように、5モル%のGe(OCH34
を含むSi(OCH341モルに対して4.5モルのCH3
OHを加え、これに4モルの0.01NのHC水溶液
を攪拌しながら加えて加水分解反応を完了させ
た。ついで、この溶液に1N−NH4OHを加え、
アンモニア濃度が約1/100〜1/10になるようにし
てゲル化させた。このゲルを70℃の恒温槽にて徐
徐に乾燥したところ、かさ密度が約0.6g/cm3
乾燥ゲルが得られた。比較のためアンモニア調製
しないでゲル化させたゲルを乾燥させたところ、
ゲルかさ密度は1.1g/cm3であつた。これらの乾
燥ゲルを、電気炉にて1300℃まで昇温したとこ
ろ、アルカリ調製ゲルは透明ガラス体(ガラス
A)となつた。また、アンモニア調製しないゲル
も1100℃では透明ガラス体(ガラスB)であつた
が、1300℃まで昇温すると発泡した。
Example As shown in Figure 2, 5 mol% Ge(OCH 3 ) 4
4.5 mol of CH 3 per 1 mol of Si(OCH 3 ) 4 containing
OH was added, and to this was added 4 molar 0.01N HC aqueous solution with stirring to complete the hydrolysis reaction. Then, 1N-NH 4 OH was added to this solution,
Gelation was carried out at an ammonia concentration of approximately 1/100 to 1/10. When this gel was slowly dried in a constant temperature bath at 70°C, a dried gel with a bulk density of about 0.6 g/cm 3 was obtained. For comparison, we dried the gel without preparing ammonia.
The gel bulk density was 1.1 g/cm 3 . When these dried gels were heated to 1300° C. in an electric furnace, the alkali-prepared gels became transparent glass bodies (glass A). Furthermore, the gel without ammonia preparation was a transparent glass body (glass B) at 1100°C, but foamed when the temperature was raised to 1300°C.

他方、比較のために、上記のGe(OCH34を5
モル%含有するSi(OCH34を0.01NのNH4OH水
溶液を用いて直接加水分解し、ゲルを作成したと
ころ、かさ密度が0.59g/cm3の乾燥ゲルが得られ
た。これを同様に昇温焼結したところ、1300℃で
透明ガラス体(ガラスC)が得られた。
On the other hand, for comparison, the above Ge(OCH 3 ) 4 is
When a gel was prepared by directly hydrolyzing Si(OCH 3 ) 4 containing mol % using a 0.01N NH 4 OH aqueous solution, a dry gel with a bulk density of 0.59 g/cm 3 was obtained. When this was similarly heated and sintered, a transparent glass body (glass C) was obtained at 1300°C.

次にガラスA,ガラスB,ガラスCの光学特性
を調べるために、約50μmの厚みに切断し光学研
磨し、波長210〜360nmの領域で光透過率を測定
したところ、ガラスA,Bはいずれも光透過率は
100%であつたが、ガラスCは242nmにピークを
もつ大きな吸収が表われた。このピークは文献に
よればガラス中にGeOが存在する時に表われる
ピークであり、ガラスCは、A,Bにくらべて均
質度が低いことがわかる。したがつて、酸性の水
溶液で加水分解した後、アンモニア水溶液でゲル
化させて作成したガラスAは、高温でも発泡する
ことなくかつ均質度の高いガラスであることがわ
かる。
Next, in order to examine the optical properties of Glass A, Glass B, and Glass C, we cut them into approximately 50 μm thick pieces, optically polished them, and measured their light transmittance in the wavelength range of 210 to 360 nm. The light transmittance is
However, glass C exhibited large absorption with a peak at 242 nm. According to the literature, this peak appears when GeO is present in the glass, and it can be seen that glass C has a lower homogeneity than A and B. Therefore, it can be seen that Glass A, which was prepared by hydrolyzing with an acidic aqueous solution and then gelling with an ammonia aqueous solution, is a highly homogeneous glass that does not foam even at high temperatures.

以上の実施例では第2の成分としてGe(OCH3
4を用いたが、Geの代りに、A,Sb,Ta,Ti,
Zr,Ga,Nbなどのうち一種あるいは二種以上の
添加元素を用いる場合も本発明の方法が適用でき
る。
In the above examples, Ge (OCH 3 ) was used as the second component.
4 was used, but instead of Ge, A, Sb, Ta, Ti,
The method of the present invention can also be applied when one or more additive elements such as Zr, Ga, and Nb are used.

〔発明の効果〕〔Effect of the invention〕

以上説明したとおり、本発明によれば、きわめ
て均質でかつかさ密度の低いゲルが作成できるの
で、これを焼結することにより、発泡のない、均
質な複数成分からなるガラス体が製造できる。
As explained above, according to the present invention, a gel that is extremely homogeneous and has a low bulk density can be created, and by sintering this gel, a homogeneous glass body made of multiple components without foaming can be manufactured.

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

第1図は従来のプロセスの工程を示す説明図、
第2図は本発明のプロセスの工程を示す説明図で
ある。 1……アルコキシド+水又はHC又はNH4
OH水溶液+アルコール、2,8……ゲル、3,
3′,3″,3……ゲル作成容器、4,4′,9,
9′……乾燥ゲル、5,5′……電気炉、6……ア
ルコキシド+HC水溶液+アルコール、7……
アルカリ調製した加水分解溶液。
Figure 1 is an explanatory diagram showing the steps of a conventional process;
FIG. 2 is an explanatory diagram showing the steps of the process of the present invention. 1...Alkoxide + water or HC or NH 4
OH aqueous solution + alcohol, 2, 8...gel, 3,
3', 3'', 3... Gel preparation container, 4, 4', 9,
9'...Dried gel, 5,5'...Electric furnace, 6...Alkoxide + HC aqueous solution + alcohol, 7...
Alkaline prepared hydrolysis solution.

Claims (1)

【特許請求の範囲】[Claims] 1 シリコンアルコキシドまたは他の金属アルコ
キシドを含有するシリコンアルコキシドを、水ま
たは金属イオンを含有する水溶液で加水分解し、
ゲル化して乾燥せしめて成る添加形シリカゲルの
製造方法において、中性もしくは酸性条件で加水
分解を行なわしめ、かつアルカリ性の条件でゲル
化せしめることを特徴とする添加形シリカゲルの
製造方法。
1. Hydrolyzing silicon alkoxide or silicon alkoxide containing other metal alkoxides with water or an aqueous solution containing metal ions,
1. A method for producing additive silica gel which is formed by gelling and drying, the method comprising carrying out hydrolysis under neutral or acidic conditions and gelling under alkaline conditions.
JP13275883A 1983-07-22 1983-07-22 Production of additive-type silica gel Granted JPS6027611A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13275883A JPS6027611A (en) 1983-07-22 1983-07-22 Production of additive-type silica gel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13275883A JPS6027611A (en) 1983-07-22 1983-07-22 Production of additive-type silica gel

Publications (2)

Publication Number Publication Date
JPS6027611A JPS6027611A (en) 1985-02-12
JPH0466811B2 true JPH0466811B2 (en) 1992-10-26

Family

ID=15088864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13275883A Granted JPS6027611A (en) 1983-07-22 1983-07-22 Production of additive-type silica gel

Country Status (1)

Country Link
JP (1) JPS6027611A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3873512T2 (en) * 1988-02-19 1992-12-03 Tohru Yamamoto CATALYST FOR THE SOL GEL METHOD USING A METAL ALKOXIDE AND THE SOL GEL METHOD USING OXIDE.
JP4912190B2 (en) * 2007-03-15 2012-04-11 独立行政法人科学技術振興機構 Method for producing porous silica gel and silica glass

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59116135A (en) * 1982-12-23 1984-07-04 Seiko Epson Corp Silica glass manufacturing method

Also Published As

Publication number Publication date
JPS6027611A (en) 1985-02-12

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