JPH0283220A - Production of glass body - Google Patents
Production of glass bodyInfo
- Publication number
- JPH0283220A JPH0283220A JP23535188A JP23535188A JPH0283220A JP H0283220 A JPH0283220 A JP H0283220A JP 23535188 A JP23535188 A JP 23535188A JP 23535188 A JP23535188 A JP 23535188A JP H0283220 A JPH0283220 A JP H0283220A
- Authority
- JP
- Japan
- Prior art keywords
- gel
- surfactant
- liquid
- contact
- drying
- 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
- 239000011521 glass Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 239000004094 surface-active agent Substances 0.000 claims abstract description 29
- 239000011148 porous material Substances 0.000 claims abstract description 15
- 150000002902 organometallic compounds Chemical class 0.000 claims abstract description 8
- 238000001035 drying Methods 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 6
- 238000005245 sintering Methods 0.000 claims description 3
- 239000000693 micelle Substances 0.000 abstract description 4
- 238000003980 solgel method Methods 0.000 abstract description 3
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002736 nonionic surfactant Substances 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract 4
- 238000001354 calcination Methods 0.000 abstract 1
- 238000005336 cracking Methods 0.000 abstract 1
- 239000002563 ionic surfactant Substances 0.000 abstract 1
- -1 methyl orthosilicate Chemical class 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 63
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 9
- 235000011114 ammonium hydroxide Nutrition 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 239000002280 amphoteric surfactant Substances 0.000 description 7
- 239000011240 wet gel Substances 0.000 description 7
- 239000000377 silicon dioxide Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 4
- 239000007863 gel particle Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- HFGHRUCCKVYFKL-UHFFFAOYSA-N 4-ethoxy-2-piperazin-1-yl-7-pyridin-4-yl-5h-pyrimido[5,4-b]indole Chemical compound C1=C2NC=3C(OCC)=NC(N4CCNCC4)=NC=3C2=CC=C1C1=CC=NC=C1 HFGHRUCCKVYFKL-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 239000003945 anionic surfactant Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- AYOOGWWGECJQPI-NSHDSACASA-N n-[(1s)-1-(5-fluoropyrimidin-2-yl)ethyl]-3-(3-propan-2-yloxy-1h-pyrazol-5-yl)imidazo[4,5-b]pyridin-5-amine Chemical compound N1C(OC(C)C)=CC(N2C3=NC(N[C@@H](C)C=4N=CC(F)=CN=4)=CC=C3N=C2)=N1 AYOOGWWGECJQPI-NSHDSACASA-N 0.000 description 2
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- XULSCZPZVQIMFM-IPZQJPLYSA-N odevixibat Chemical compound C12=CC(SC)=C(OCC(=O)N[C@@H](C(=O)N[C@@H](CC)C(O)=O)C=3C=CC(O)=CC=3)C=C2S(=O)(=O)NC(CCCC)(CCCC)CN1C1=CC=CC=C1 XULSCZPZVQIMFM-IPZQJPLYSA-N 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- KMIOJWCYOHBUJS-HAKPAVFJSA-N vorolanib Chemical compound C1N(C(=O)N(C)C)CC[C@@H]1NC(=O)C1=C(C)NC(\C=C/2C3=CC(F)=CC=C3NC\2=O)=C1C KMIOJWCYOHBUJS-HAKPAVFJSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/12—Other methods of shaping glass by liquid-phase reaction processes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
Description
本発明はガラス体の製造方法に関し、特に、有機金属化
合物原料の加水分解・縮重合により溶液をゲル化させた
後、この得られたゲル体を乾燥、焼結してガラス体とす
る、通称ゾル−ゲル法と呼ばれるガラス体の製造方法に
間する。The present invention relates to a method for producing a glass body, and in particular to a method for producing a glass body, in which a solution is gelled by hydrolysis and polycondensation of an organic metal compound raw material, and then the resulting gel body is dried and sintered to form a glass body. A method for manufacturing glass bodies called the sol-gel method was used.
有機金属化合物を用いたゾル−ゲル法によるガラス製品
の製造においては、溶媒の蒸発による体積収縮が激しく
、ゲル体の乾燥工程でクラ・ンクが発生しやすいという
大きな問題点があった。これを防ぐには、乾燥速度を抑
えて数週閏から数カ月かけて、ゆっくりと乾燥を行う方
法が知られている。しかしながら、上記方法では製造に
要する時間が長くなり、産業上の利用が事実上、不可能
となってしまう。
近年、この問題を解決するために、いくつかの方策が提
案されている0代表的なものは■原料溶液にシリカ微粉
末を添加してクラックを抑える方法(例えば、特開昭5
9−92924)、■ゲル体を臨界条件下で乾燥するこ
とによりクラックのないゲル体を得る。方法(例えば、
特開昭57−209817 )、■溶媒に蒸発速度の遅
いホルムアミド等を用いる方法(例えば、L、L、He
nchら、 Mat、Res、Soc、Symp、P
roc、、 32.47(1984))、■ゲル体中
に残留しているアルコキシル基を水酸基に置換した後に
乾燥を行う方法(例えば、T、Mizunoら、第4回
ゾルゲル国際ワークショップ、1987年、京都)であ
る。
しかしながら、上記の従来技術において、■のシリカ微
粉末を添加する方法では、クラックの発生傾向は低くな
るものの、溶液にシリカの微粉末を分散させるのに手間
がかかる上に、乾燥速度を大幅に上げることが不可能で
あるという問題点があった。また、■のゲル体を臨界条
件下で乾燥する方法では、オートクレーブを使用するた
め、設備投資が大きく、かつ生産性が悲いという問題点
があり、ざらに■の溶媒にホルムアミドを用いる方法で
は、ゲル体中に多量のホルムアミドが残留しており、こ
れが焼結工程中のゲル体にクラックを発生させるという
問題点があった。In the manufacture of glass products by the sol-gel method using organometallic compounds, there has been a major problem in that volume shrinkage is severe due to evaporation of the solvent, and cracks are likely to occur during the drying process of the gel body. To prevent this, there is a known method of slowing down the drying speed and drying slowly over several weeks to several months. However, the above method takes a long time to manufacture, making industrial use virtually impossible. In recent years, several measures have been proposed to solve this problem.The most representative ones are: 1) Adding fine silica powder to the raw material solution to suppress cracks (for example, Japanese Patent Laid-open No. 5
9-92924), (2) A crack-free gel body is obtained by drying the gel body under critical conditions. method (e.g.
(Japanese Patent Application Laid-Open No. 57-209817), (2) A method using formamide, etc., which has a slow evaporation rate as a solvent (for example, L, L, He
nch et al., Mat, Res, Soc, Symp, P
roc, 32.47 (1984)), ■ a method of replacing the alkoxyl groups remaining in the gel body with hydroxyl groups and then drying (for example, T., Mizuno et al., 4th Sol-Gel International Workshop, 1987) , Kyoto). However, in the above-mentioned conventional technology, although the method of adding fine silica powder reduces the tendency for cracks to occur, it takes time and effort to disperse the fine silica powder in the solution, and it significantly slows down the drying speed. The problem was that it was impossible to raise the In addition, the method (2) of drying the gel body under critical conditions requires a large investment in equipment due to the use of an autoclave, and has the problem of poor productivity. However, there was a problem in that a large amount of formamide remained in the gel body, which caused cracks in the gel body during the sintering process.
本発明者らが帰室じている■の方法は、ゲル体を、その
細孔を満たしている液体の含水率より高い含水率の液体
に浸漬してアルコキシル基を水酸基へall!L、た後
乾燥する方法であり、簡便な方法ながら、非常に効果が
ある。また、この方法において使用できる液体の液性は
、酸性から塩基性まで幅広い、特に塩基性液体に浸漬処
理したゲル体は、同時にその比表面積が小さくなり、っ
まり細孔径が大きくなり焼結性が向上するのでガラスを
容易に得ることができることがわがフでいる(例えば、
T、Mizunoら、 J、 Man−Cryst
、 5olids、出。
236(198B)) 、 ところが、その後の本発
明者らの研究から、ゲル体を大きくすると塩基性液体に
浸漬した場合、乾燥時にクラックが発生し易くなること
がわかった。
本発明は上記の従来技術に鑑み、塩基性液体に浸漬した
大型ゲル体の焼結性を維持し、かつ乾燥時のクラックを
抑制する方法を提供するものである。The method (2), which the present inventors are working on, is to immerse the gel body in a liquid with a water content higher than that of the liquid filling the pores of the gel to transform all the alkoxyl groups into hydroxyl groups. Although it is a simple method, it is very effective. In addition, the properties of the liquid that can be used in this method range from acidic to basic. In particular, gel bodies immersed in basic liquids have a smaller specific surface area, a larger pore size, and a higher sinterability. We are proud that we can easily obtain glass by improving the
T, Mizuno et al., J, Man-Cryst
, 5olids, out. 236 (198B)) However, subsequent research by the present inventors revealed that when the gel body is made larger, cracks are more likely to occur during drying when it is immersed in a basic liquid. In view of the above-mentioned prior art, the present invention provides a method for maintaining the sinterability of a large gel body immersed in a basic liquid and suppressing cracks during drying.
本発明は、上記問題点を解決するためになされたもので
あフて、有機金属化合物を含む原料溶液をゲル化してゲ
ル体を作製し、該ゲル体の細孔中の液体の含水率より高
い含水率の塩基性液体と該ゲル体とを接触させた後、乾
燥・vE結してガラス体を製造する方法において、乾燥
前のゲル体を、界面活性剤を含有する溶液と接触させて
いる。
該ゲル体を、界面活性剤を含有する溶液と接触させる方
法としては、■該ゲル体の細孔中の液体の含水率より高
い含水率の塩基性液体と該ゲル体とを接触させる際に、
該塩基性液体に界面活性剤を添加しておく方法、■界面
活性剤を含有する溶1αとゲル体とを接触させた後、引
続き塩基性液体と該ゲル体とを接触させる方法、■塩基
性液体とゲル体とを接触させた後、界面活性剤を含有す
る溶液と該ゲル体とを接触させる方法、■塩基性液体と
ゲル体と接触させた後、該塩基性液体に界面活性剤を添
加し該ゲル体と接触させる方法、等が例示できる。
塩基性液体のp Hは、特に限定されるものではないが
、8より小さいとゲル細孔径増大効果が顕著ではなく、
また12より大きいとゲル溶解が著しく起こり、ゲルの
強度が低下するので好ましくない、よって、塩基性液体
のPHは8以上12以下であることが好ましい。
ゲル体と界面活性剤との接触により、ゲル体縞孔中の液
体の表面張力が小さくなる。該’a液に添加する界面活
性剤の量は、臨界ミセル濃度より多いことが好ましいが
、臨界ミセル濃度より多くても表面張力は著しく低下し
ないので、過剰の界面活性剤は無駄となる。また、あま
り界面活性剤が多いとゲル焼結時に界面活性剤が残留し
、ガラスの純度が低下する。よって、界面活性剤濃度の
上限は臨界ミセル濃度以上のlvt%が好ましい。添加
する界面活性剤は、それ以ドであっ′Cも、蛇燥工稈中
に濃縮され効果を発揮する。実際に顕著な効果を得るた
めには、少なくとも0. OO01vt%含有さUる
ことが好ましい。
界面活性剤の種類については、とのようなものでもある
程度の効果を発揮する。しかし、陰イオン系界面活性剤
は、溶出したシリカ等のゲル成分と吸着反応を起こし、
ゲル粒子の成長を阻害するので好ましくない、また、陰
イオン系界面活性剤は、乾燥歩留が低いため好ましくな
い0両性界面活性剤または非イオン系W面活性剤では、
乾燥歩留が高く、これらの界面活性剤を用いるのがより
好ましい。
ゲル体と、界面活性剤を含む塩基性液体とを接触させる
温度は、特に限定されるものではないが、あまり、低温
であると液体の置換反応及びゲル粒子成長反応が緩慢と
なり、処理時閉が長くなる。
また高温であると、溶媒の沸点を越え内圧が上昇するた
め、高価な耐圧容器が必要となる。従って20〜80℃
が好ましい。
また、ゲル体と、界面活性剤を含む塩基性液体とを接触
させる時間も、特に限定されるものではないが、あまり
短いとゲル粒子の成長が不完全となり、ゲル表層と内部
との不均一も顕著となるので、3時間以上が好ましい、
接触時間が、あまり長いと生産性が低下し、またゲル溶
解が次第に起こるなどの弊害も現れるので、上限は10
000時間ましい。The present invention has been made to solve the above-mentioned problems, and involves producing a gel body by gelling a raw material solution containing an organometallic compound, and determining the water content of the liquid in the pores of the gel body. In the method of producing a glass body by bringing the gel body into contact with a basic liquid having a high water content and then drying and vE-curing, the gel body before drying is brought into contact with a solution containing a surfactant. There is. The method of bringing the gel body into contact with a solution containing a surfactant includes (1) bringing the gel body into contact with a basic liquid having a water content higher than the water content of the liquid in the pores of the gel body; ,
A method in which a surfactant is added to the basic liquid; (2) a method in which a solution 1α containing a surfactant is brought into contact with a gel body, and then a basic liquid is brought into contact with the gel body; (2) a base. A method of bringing a basic liquid into contact with a gel body and then contacting the gel body with a solution containing a surfactant; Examples include a method of adding and bringing into contact with the gel body. The pH of the basic liquid is not particularly limited, but if it is less than 8, the effect of increasing the gel pore size will not be significant.
Moreover, if it is larger than 12, gel dissolution will occur significantly and the strength of the gel will decrease, which is not preferable. Therefore, it is preferable that the pH of the basic liquid is 8 or more and 12 or less. Contact between the gel body and the surfactant reduces the surface tension of the liquid in the striped pores of the gel body. The amount of surfactant added to the liquid 'a' is preferably greater than the critical micelle concentration, but even if the amount is greater than the critical micelle concentration, the surface tension will not drop significantly, so excess surfactant will be wasted. Furthermore, if the amount of surfactant is too large, the surfactant will remain during gel sintering and the purity of the glass will decrease. Therefore, the upper limit of the surfactant concentration is preferably lvt% equal to or higher than the critical micelle concentration. The added surfactant is also concentrated in the culm and exerts its effect. In order to obtain a really noticeable effect, at least 0. It is preferable to contain OO01vt%. Regarding the type of surfactant, surfactants such as and can also have some effect. However, anionic surfactants cause adsorption reactions with eluted gel components such as silica,
Anionic surfactants are undesirable because they inhibit the growth of gel particles; amphoteric surfactants or nonionic W surfactants are undesirable because they have a low drying yield;
It is more preferable to use these surfactants because of their high drying yield. The temperature at which the gel body is brought into contact with the basic liquid containing a surfactant is not particularly limited, but if the temperature is too low, the liquid displacement reaction and gel particle growth reaction will be slow, resulting in closure during processing. becomes longer. Moreover, if the temperature is high, the internal pressure will rise beyond the boiling point of the solvent, and an expensive pressure-resistant container will be required. Therefore 20~80℃
is preferred. In addition, the time period for which the gel body is brought into contact with the basic liquid containing a surfactant is not particularly limited, but if it is too short, the growth of the gel particles will be incomplete, resulting in non-uniformity between the surface layer and the inside of the gel. 3 hours or more is preferable.
If the contact time is too long, productivity will decrease and problems such as gradual gel dissolution will occur, so the upper limit is 10
000 hours.
乾燥中のゲル体にクラックを発生させる力は、気−液一
固界面で生ずる毛細管力であり、これは毛細管力ΔP、
ゲルの細孔半径r、纏孔を満たしている液体の表面張力
γ、ゲル纏孔中の液体とゲルの接触角θを用いて、次の
ように示されることが知られている。
上記式(1)から、ゲル細孔中の液体の表面張力を小さ
くすると、乾燥中のクラックを抑制することができる。
含水率の高い液体の表面張力は数十dyn/c■である
が、界面活性剤を添加することで、1/2〜173程度
に減少させることができる。
塩基性液体にゲ、ルを浸漬すると、ゲル粒子径の増大が
認められる。この結果、ゲルの細孔径が大きくなり、乾
燥中のゲルの耐クラツク性が向上する。また、そればか
りでなく、ゲルの焼結性も向上し、容易にガラス化する
ことができるようになる。
界面活性剤の作用は、ゲル細孔中液体の表面張力を低下
させることであるが、本発明における塩基性液体を使用
する状況では、特に、両性界面活性剤または非イオン系
界面活性剤を用いた場合、クラック抑制に一層の効果が
ある。
以上のように、本発明によれば、界面活性剤を含む塩基
性液体にゲル体を接触させることで、クラックの発生原
因である毛細管力を低減でき、クラックを発生させるこ
となく素早く乾燥を行うことができる。かつゲル細孔径
が大きくなるので焼結性のよいゲル体を得ることができ
るようになる。
本発明の方法は、有機金属化合物を含む液体から作製し
たゲル体であれば、どのような組成のゲル体にも適用で
きる。
以下、実施例に基づいて本発明を更に詳しく説明する。The force that causes cracks in the drying gel body is the capillary force that occurs at the gas-liquid-solid interface, and this is the capillary force ΔP,
It is known that it can be expressed as follows using the pore radius r of the gel, the surface tension γ of the liquid filling the pores, and the contact angle θ between the liquid in the gel pores and the gel. From the above formula (1), by reducing the surface tension of the liquid in the gel pores, cracks during drying can be suppressed. Although the surface tension of a liquid with a high water content is several tens of dyn/c, it can be reduced to about 1/2 to 173 by adding a surfactant. When a gel is immersed in a basic liquid, an increase in the gel particle size is observed. As a result, the pore size of the gel becomes larger and the crack resistance of the gel during drying is improved. In addition, the sinterability of the gel is improved, and it becomes possible to vitrify it easily. The action of surfactants is to reduce the surface tension of the liquid in the gel pores, but in the context of using basic liquids in the present invention, it is especially important to use amphoteric surfactants or nonionic surfactants. If it is, it will be even more effective in suppressing cracks. As described above, according to the present invention, by bringing a gel body into contact with a basic liquid containing a surfactant, the capillary force that causes cracks can be reduced, and drying can be performed quickly without causing cracks. be able to. In addition, since the gel pore diameter becomes large, a gel body with good sinterability can be obtained. The method of the present invention can be applied to gel bodies of any composition as long as they are produced from liquids containing organometallic compounds. Hereinafter, the present invention will be explained in more detail based on Examples.
実施例−1〜4
市販のオルト珪酸メチル、エタノールおよび水を体積比
でl+o、43:1.83の割合で混合し、約30分明
攪拌して、透明な液体を得た。この液体260m1を、
−辺が15cmのテフロンコーティングを施したステン
レス製容器に入れて密閉し、60℃で24時間、ゲル化
及び養生を行った。このウェットゲルを、第1表に示し
たような各種界面活性剤を0.02vt%含む0.IN
アンモニア水260m1に60℃で24時間浸漬した。
その後液体を捨て、80℃で乾燥を行った。乾燥の初期
は0、 2%の間口率の蓋をして24WIt間保持し、
その後、蓋を除去して、18時間乾燥を行い、約85m
m角、7 m m厚の乾燥ゲルを得た。乾燥歩留を第1
表に示す、その後、得られた乾燥ゲル°を、1000〜
1100℃で熱処理したところ、いずれのゲルも、約6
0mm角、5mm厚の透明なガラスとなった。
比較例−1〜2
本発明の効果を確認するため、実施例−1〜4と同様に
して得たウェットゲルを、
比較例1:0.INアンモニア水
比較例2:水+両性界面活性剤(0,02wt%)の水
溶液にそれぞれ浸漬し、上記実施例と同一条件で浸漬処
理を行い、乾燥、焼結を行った。結果を111表に示す
。
処理液中に界面活性剤が含まれていない(比較例1)な
らば乾燥歩留が低く、アンモニアが含ま第 1
表
第 1
表(つづき)
れていない(比較例2)ならば焼結性が悉く、この条件
では発泡した。よって、上記実施例および比較例から、
本発明の効果が顕著であることがわかる。
実施例−5
実施例−1−4と同様にして得られたウェットゲルを、
0.INアンモニア水260m1に浸漬し、60℃、1
2時間処理した。その後、両性界面活性剤を、濃度がO
−02wt%となるように添加して、60℃、 12時
間放置した。このゲルを、実施例−1〜4と同様にして
乾燥を行ったところ、乾燥歩留は、実施例3と同様、8
5%であった。
また、この乾燥ゲルを、実施例−1〜4と同じ1000
〜1100℃で熱処理したところ、透明なガラスとなっ
た。
実施例−6
市販のオルト珪酸メチル、エタノール、および水を、l
:o、43:1.83の体積比で混合した溶液に、市販
のT i (OCnH*) 4を、焼成後にチタニアと
して5wt%含まれるように添加し、混合溶液を作製し
、実施例−1〜4と同様にしてウェットゲルを得た。こ
のウェットゲルを、両性界面活性剤を0゜002wt%
含む0.INアンモニア水260 m lに60℃で2
4時間浸漬した。その後、実施例−1〜4と同様にして
乾燥を行った。乾燥歩留を、第2表に示す、この乾燥ゲ
ルは、1100〜1200℃の熱処理により容易にガラ
ス化できた(第2表参照)。
第 2
表
比較例−3〜4
実施例−6と同様にして得たウェットゲルを、比較例3
:0.INアンモニア水
比較例4: 水子両性界面活性剤(0,002wt%)
の水溶液にそれぞれ浸漬し、実施例−6と同一条件で浸
漬処理を行い、乾燥、焼結を行った。結果を第2表に示
す。
実施例−7
実施例−1〜4と同様にして得られたウェットゲルを、
0.INアンモニア水260 m lに浸漬し、60℃
、24時間浸漬処理した。その後、アンモニア水を捨て
、0. 02wt%の両性界面活性剤水溶液260m1
に60℃、24時間浸漬した。
その後、液体を捨て、実施例−1〜4と同様にして乾燥
を行ったところ、乾燥歩留は、80%であフた。また、
この乾燥ゲルを、実施例−1〜4と同じ条件で熱処理し
たところ、透明なガラスとなった。
実施例−8
実施例−7の■アンモニア水処理と■界面活性剤処理の
順番を逆にした以外は実施例−7の手順を用いてゲル体
を作成した。乾燥歩留は、50%であった。また、この
乾燥ゲルを、実施例−1〜4と同じ条件で熱処理したと
ころ、透明なガラスとなった。
上記実施例においては、有機金属化合物を含む原料溶液
として、シリカ微粉末等を添加していない通常のゾル−
ゲル溶液を用いているが、本発明は上記に限らず、シリ
カ微粉末等を含む有機金属化合物を含む原料溶液を用い
てもかまわない。Examples 1 to 4 Commercially available methyl orthosilicate, ethanol, and water were mixed at a volume ratio of l+o, 43:1.83, and stirred for about 30 minutes to obtain a transparent liquid. 260ml of this liquid,
- It was placed in a Teflon-coated stainless steel container with sides of 15 cm and sealed, and gelatinized and cured at 60° C. for 24 hours. This wet gel was mixed with 0.00% of the various surfactants shown in Table 1 containing 0.02vt%. IN
It was immersed in 260 ml of ammonia water at 60°C for 24 hours. Thereafter, the liquid was discarded and the product was dried at 80°C. At the beginning of drying, cover with a lid with a frontage ratio of 0.2% and hold for 24 WIt.
After that, the lid was removed and dried for 18 hours. Approximately 85 m
A dried gel measuring m square and 7 mm thick was obtained. Drying yield is the first priority
Then, the obtained dry gel ° as shown in the table is 1000 ~
When heat treated at 1100°C, all gels had a
The resulting glass was 0 mm square and 5 mm thick. Comparative Examples 1 to 2 In order to confirm the effects of the present invention, wet gels obtained in the same manner as Examples 1 to 4 were prepared in Comparative Example 1:0. IN Ammonia Water Comparative Example 2: Each sample was immersed in an aqueous solution of water + amphoteric surfactant (0.02 wt%), subjected to immersion treatment under the same conditions as in the above example, and then dried and sintered. The results are shown in Table 111. If the treatment liquid does not contain a surfactant (Comparative Example 1), the drying yield will be low, and if it does not contain ammonia (Comparative Example 2), the drying yield will be low. All foamed under these conditions. Therefore, from the above examples and comparative examples,
It can be seen that the effects of the present invention are remarkable. Example-5 Wet gel obtained in the same manner as Example-1-4,
0. Immersed in 260ml of IN ammonia water, 60℃, 1
It was treated for 2 hours. Then, add an amphoteric surfactant to a concentration of O
-02 wt% and left at 60°C for 12 hours. When this gel was dried in the same manner as in Examples 1 to 4, the drying yield was 8.
It was 5%. In addition, this dry gel was heated to 1000
When heat treated at ~1100°C, a transparent glass was obtained. Example-6 Commercially available methyl orthosilicate, ethanol, and water were
:o, 43:1.83 volume ratio, commercially available Ti(OCnH*) 4 was added so as to contain 5 wt% as titania after firing to prepare a mixed solution, and Example- Wet gels were obtained in the same manner as in 1 to 4. This wet gel was mixed with 0°002wt% of amphoteric surfactant.
Including 0. 260 ml of IN ammonia water at 60°C.
Soaked for 4 hours. Thereafter, drying was performed in the same manner as in Examples 1 to 4. The drying yield is shown in Table 2. This dried gel could be easily vitrified by heat treatment at 1100 to 1200°C (see Table 2). Table 2 Comparative Examples-3 to 4 Wet gels obtained in the same manner as in Example-6 were used in Comparative Example 3.
:0. IN Ammonia water comparative example 4: Water amphoteric surfactant (0,002wt%)
The samples were each immersed in an aqueous solution of the above, subjected to the immersion treatment under the same conditions as in Example 6, and then dried and sintered. The results are shown in Table 2. Example 7 Wet gel obtained in the same manner as Examples 1 to 4,
0. Immerse in 260 ml of IN ammonia water at 60°C.
, soaked for 24 hours. After that, discard the ammonia water and remove the ammonia water. 02wt% amphoteric surfactant aqueous solution 260ml
It was immersed in water at 60°C for 24 hours. Thereafter, the liquid was discarded and drying was performed in the same manner as in Examples 1 to 4, and the drying yield was 80%. Also,
When this dried gel was heat-treated under the same conditions as Examples 1 to 4, it became transparent glass. Example-8 A gel body was prepared using the procedure of Example-7 except that the order of (1) ammonia water treatment and (2) surfactant treatment in Example-7 was reversed. The drying yield was 50%. Moreover, when this dried gel was heat-treated under the same conditions as Examples 1 to 4, it became transparent glass. In the above examples, the raw material solution containing the organometallic compound is a normal sol to which fine silica powder etc. are not added.
Although a gel solution is used, the present invention is not limited to the above, and a raw material solution containing an organometallic compound containing fine silica powder or the like may be used.
本発明によれば、上記実施例および比較例から明らかな
ように、クラックを発生させずに、焼結性の非常によい
乾燥ゲルを、短時間で得ることができるようになる。
本発明は、ゲル体自身に対する制限がほとんどないので
、いかなる成分、組成のガラスにも適用可能である。
特許出願人 日本板硝子株式会社
で二部5・1According to the present invention, as is clear from the above Examples and Comparative Examples, a dry gel with very good sinterability can be obtained in a short time without generating cracks. Since the present invention has almost no restrictions on the gel body itself, it can be applied to glasses of any components and compositions. Patent applicant Nippon Sheet Glass Co., Ltd. 2nd Division 5.1
Claims (1)
体を作製し、該ゲル体を、該ゲル体の細孔中の液体の含
水率より高い含水率の塩基性液体と接触させた後、乾燥
・焼結してガラス体を製造する方法において、乾燥前の
ゲル体を、界面活性剤を含有する溶液と接触させること
を特徴とするガラス体の製造法。(1) After producing a gel body by gelling a raw material solution containing an organometallic compound, and bringing the gel body into contact with a basic liquid having a water content higher than the water content of the liquid in the pores of the gel body. A method for producing a glass body by drying and sintering, the method comprising bringing the gel body before drying into contact with a solution containing a surfactant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23535188A JPH0283220A (en) | 1988-09-20 | 1988-09-20 | Production of glass body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23535188A JPH0283220A (en) | 1988-09-20 | 1988-09-20 | Production of glass body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0283220A true JPH0283220A (en) | 1990-03-23 |
Family
ID=16984802
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23535188A Pending JPH0283220A (en) | 1988-09-20 | 1988-09-20 | Production of glass body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0283220A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0719735A1 (en) * | 1994-12-29 | 1996-07-03 | AT&T Corp. | Fabrication of a thin sheet by a sol-gel process |
-
1988
- 1988-09-20 JP JP23535188A patent/JPH0283220A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0719735A1 (en) * | 1994-12-29 | 1996-07-03 | AT&T Corp. | Fabrication of a thin sheet by a sol-gel process |
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