JPH0226835A - Method for manufacturing porous glass - Google Patents
Method for manufacturing porous glassInfo
- Publication number
- JPH0226835A JPH0226835A JP17790288A JP17790288A JPH0226835A JP H0226835 A JPH0226835 A JP H0226835A JP 17790288 A JP17790288 A JP 17790288A JP 17790288 A JP17790288 A JP 17790288A JP H0226835 A JPH0226835 A JP H0226835A
- Authority
- JP
- Japan
- Prior art keywords
- sol
- glass
- gel
- porous glass
- blowing agent
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000005373 porous glass Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title description 4
- 239000011521 glass Substances 0.000 claims abstract description 10
- 239000004604 Blowing Agent Substances 0.000 claims abstract description 9
- 238000003980 solgel method Methods 0.000 claims abstract description 7
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 238000005245 sintering Methods 0.000 claims description 10
- 239000004088 foaming agent Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 3
- 239000004156 Azodicarbonamide Substances 0.000 abstract description 4
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 abstract description 4
- 235000019399 azodicarbonamide Nutrition 0.000 abstract description 4
- 238000005187 foaming Methods 0.000 abstract description 4
- 239000011148 porous material Substances 0.000 description 12
- 239000000499 gel Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011494 foam glass Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000011240 wet gel Substances 0.000 description 2
- XTIFKYBZJZGLPQ-UHFFFAOYSA-N (sulfoamino)sulfamic acid Chemical compound OS(=O)(=O)NNS(O)(=O)=O XTIFKYBZJZGLPQ-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- 108010093096 Immobilized Enzymes Proteins 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 239000005388 borosilicate glass Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/006—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route
-
- 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
-
- 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
- C03C11/00—Multi-cellular glass ; Porous or hollow glass or glass particles
- C03C11/007—Foam glass, e.g. obtained by incorporating a blowing agent and heating
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、高圧・高温下でのガス分離や、海水の淡水化
の触媒及び固定化酵素や無機触媒の担体等に使われる多
孔質ガラスの製造方法に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to porous glass used for gas separation under high pressure and high temperature, as a catalyst for desalination of seawater, and as a carrier for immobilized enzymes and inorganic catalysts. Relating to a manufacturing method.
[従来の技術]
従来の多孔質ガラスの製造方法を、第2図に示す。Na
、O−B10.−3 i 02からなる原料を調整後、
約1500℃の高温下で溶融し、さらに800℃〜11
00℃の温度で管・板などの形状に成形する。この時得
られるホウケイ酸ガラスは、未分相であるため、500
℃〜650℃の温度範囲で分相処理を行い、Na、O−
B、O,相と810、相の2相に分離される。この分相
ガラスに硝酸や塩酸などで酸処理を行うと、酸に溶解し
ゃすいNa、O−B、O,相は溶出してゆき、S10、
相のみが残存する。Na、O−B、O8相と810、相
はガラス内で複雑に絡み合っているため、残存するS1
0.ガラスは、無数の連続した細孔を持つ多孔質ガラス
である。[Prior Art] A conventional method for manufacturing porous glass is shown in FIG. Na
, O-B10. -3 After adjusting the raw material consisting of 02,
Melts at a high temperature of about 1500℃, and further melts at a temperature of 800℃~11
It is formed into shapes such as tubes and plates at a temperature of 00°C. Since the borosilicate glass obtained at this time is unseparated,
Phase separation treatment was performed in the temperature range of ℃ to 650℃ to remove Na, O-
It is separated into two phases: B, O, phase and 810, phase. When this phase-separated glass is acid-treated with nitric acid or hydrochloric acid, the acid-soluble Na, O-B, and O phases are eluted, and S10,
Only the phase remains. Since the Na, OB, O8 and 810 phases are intricately intertwined within the glass, the remaining S1
0. Glass is a porous glass with countless continuous pores.
このほか、ガラス粉末とカーボンなどの発泡剤を混合し
た後高温で処理する、建材などに使用される泡ガラスの
製造方法もある。Another method for producing foam glass, which is used as building materials, involves mixing glass powder with a foaming agent such as carbon and then treating it at high temperatures.
また、ゾル−ゲル法でガラスを製造することができる。Further, glass can be manufactured by a sol-gel method.
(特開昭59−92924号公報参照)この場合、得ら
れるガラスに空孔が発生しやすいという特徴を活かして
、焼結条件を制御することにより多孔質ガラスを作る方
法も考えられている[発明が解決しようとする課題]
しかしながら、従来の製造方法では、材料を溶融した後
プレスで成形して望む形状にする必要があるため、プレ
スの金型などにより限られた形状しか出来ないなどの問
題がある。またNa、O−B、O8相中にはSiO2成
分が含まれており、酸処理のときこのS10.成分は溶
出せずに残り、細孔内でゲル状に析出して2次構造を作
る。この析出物の体積により、細孔容積は大幅に変化し
ガス分離などでは性能低下につながるという問題点を有
している。(Refer to Japanese Unexamined Patent Publication No. 59-92924.) In this case, a method has been considered to make porous glass by controlling the sintering conditions, taking advantage of the fact that pores are easily generated in the glass obtained. [Problems to be Solved by the Invention] However, in the conventional manufacturing method, it is necessary to melt the material and then press it to form the desired shape. There's a problem. Furthermore, the Na, O-B, and O8 phases contain SiO2 components, and during acid treatment, this S10. The components remain without being eluted and precipitate in the form of a gel within the pores, creating a secondary structure. This poses a problem in that the volume of the precipitates significantly changes the pore volume, leading to a decrease in performance in gas separation and the like.
泡ガラスの製造方法では、製造工程中での不純物の混入
、閉空孔が得られない、単純形状しかできないなどの問
題点を有している。The method for producing foam glass has problems such as the introduction of impurities during the production process, the inability to obtain closed pores, and the production of only simple shapes.
また従来のゾル−ゲル法では、孔径の大きな空孔が得ら
れない、焼結を途中で切り上げるため焼結体の強度が劣
るという問題点を有している。。Further, the conventional sol-gel method has problems in that pores with large pore diameters cannot be obtained and that the strength of the sintered body is poor because sintering is stopped midway through. .
本発明は、この様な問題点を解決するものであり、その
目的とするところは、形状自由度が高く、優れた強度を
有する多孔質ガラスの製造方法を提供することにある。The present invention is intended to solve these problems, and its purpose is to provide a method for producing porous glass that has a high degree of freedom in shape and has excellent strength.
[課雇を解決するための手段]
本発明の多孔質ガラスの製造方法は、ゾル−ゲル法によ
るガラスの製造において、作成したゾルに発泡剤を添加
し分散させた後、このゾルを望む形状の型に注入し、固
化・乾燥しドライゲルとし、このゲルを発泡剤の分解温
度以上に加熱し、含有している発泡剤を分解させ、さら
にこの混合物を焼結することを特徴とする。[Means for solving departmental labor problems] The method for producing porous glass of the present invention involves adding and dispersing a blowing agent to the prepared sol in the production of glass by the sol-gel method, and then shaping the sol into a desired shape. The gel is poured into a mold, solidified and dried to form a dry gel, heated to a temperature higher than the decomposition temperature of the foaming agent to decompose the foaming agent contained therein, and the mixture is further sintered.
[実施例コ
(実施例1)
代表的な多孔質ガラスについて、本発明の製造工程を第
1図に示す。[Example 1] Fig. 1 shows the manufacturing process of the present invention for a typical porous glass.
エチルシリケートを酸性下で加水分解し、これニ平均粒
子径o、os 〜0.4(μ771)のsto、711
粒子を添加、さらに発泡材料としてアゾジカルボンアミ
ドをa、1(重量%)添加した後、アンモニア水を加え
pHを4.5に合わせゾルを調整する。Ethyl silicate is hydrolyzed under acidic conditions to obtain sto, 711 particles with an average particle size o, os ~0.4 (μ771).
After adding the particles and further adding azodicarbonamide as a foaming material at 1 (wt%), aqueous ammonia is added to adjust the pH to 4.5 to prepare a sol.
このゾルを6種類のポリプロピレン製容器に入れて、密
閉状態のままゲル化を行ないウェットゲルを得る。その
後、密閉容器からウェットゲルを取り出し、2週間乾燥
させドライゲルを作成する。This sol is placed in six types of polypropylene containers, and gelation is performed in a sealed state to obtain a wet gel. Thereafter, the wet gel is taken out from the sealed container and dried for two weeks to prepare a dry gel.
このドライゲルを焼結炉にいれて、50(℃/時間)の
昇温速度で200℃まで加熱し同温度で5時間保持し、
さらに300℃に加熱し同温度で5時間保持して、添加
したアゾジカルボンアミドを完全に分解するとともに脱
吸着水処理を行なう行うことが望ましい。This dry gel was placed in a sintering furnace, heated to 200°C at a temperature increase rate of 50°C/hour, and held at the same temperature for 5 hours.
It is preferable to further heat the mixture to 300° C. and hold it at the same temperature for 5 hours to completely decompose the added azodicarbonamide and to perform desorption water treatment.
使用する発泡剤は、アゾジカルボンアミド等のアゾ系、
ジフェニルスルホン−3,31ジスルホヒドラジン等の
ヒドラジン系、N、N’−ジニトロソペンタメチレンテ
トラミン等のN−二トロン系等で代表される有機系発泡
剤及び一般の有機樹脂、カーボン、Ga003等の無機
材料の何れでもよい。The blowing agents used are azo type such as azodicarbonamide,
Organic blowing agents represented by hydrazine type such as diphenylsulfone-3,31 disulfohydrazine, N-nitrone type such as N,N'-dinitrosopentamethylenetetramine, general organic resin, carbon, Ga003, etc. Any inorganic material may be used.
得られた多孔質ガラスの寸法を表−1に、その特性を表
−2に示す。The dimensions of the obtained porous glass are shown in Table 1, and its properties are shown in Table 2.
前記ドライゲルをさらに、50(℃/時間)の昇温速度
で1000℃に加熱し、同温度で10時間保持して焼結
を行い多孔質ガラスを得る。焼結は窒素雰囲気中或は真
空中で行うが、発泡剤が完全に分解するまでの発泡・脱
ガス工程は真空中で表−2
表−3
(実施例2.)
孔径及び孔径分布を制御するために、発泡剤としてのカ
ーボンの添加量或は焼結条件をいろいろ変化させて多孔
質ガラスを作成した。本実施例における試料の形状はφ
55X 5(m)であり、その他の製造条件は実施例
1と同じとする。The dry gel is further heated to 1000° C. at a heating rate of 50° C./hour and held at the same temperature for 10 hours to perform sintering and obtain porous glass. Sintering is performed in a nitrogen atmosphere or in a vacuum, but the foaming and degassing steps until the foaming agent is completely decomposed are performed in a vacuum. In order to achieve this, porous glasses were created by varying the amount of carbon added as a blowing agent and the sintering conditions. The shape of the sample in this example is φ
55×5 (m), and other manufacturing conditions are the same as in Example 1.
ただし、カーボンの分解温度は高いため、発泡温度は8
00 ’aとする。However, since the decomposition temperature of carbon is high, the foaming temperature is 8.
00'a.
各試料の製造条件について表3に、得られた多孔質ガラ
スの特性を表4に示す。Table 3 shows the manufacturing conditions for each sample, and Table 4 shows the characteristics of the obtained porous glass.
表−4
本実施例で囮らかなよ5に、本発明の製造方法によれば
、発泡剤の添加量及び焼結温度などの製造条件を変化さ
せることにより、いろいろな特性の多孔質ガラスを得る
ことができる。(実験では1oXから100μmオーダ
ーの空孔が作成可能である。)また完全に焼結を行うた
め、得られる多孔質ガラスの強度は高く、実用上側等問
題はない。Table 4 In this example, porous glasses with various characteristics can be produced by changing the manufacturing conditions such as the amount of foaming agent added and the sintering temperature, according to the manufacturing method of the present invention. Obtainable. (In experiments, it is possible to create pores on the order of 100 μm from 10×.) Furthermore, since complete sintering is performed, the strength of the resulting porous glass is high, and there are no problems in practical terms.
第1図は、本発明の多孔質ガラスの製造方法を示す工程
図。
第2図は、従来の多孔質ガラスの製造方法を示す工程図
。
以
上
[発明の効果]
以上述べたように、本発明によれば、ゾルを任意の形状
の型に注入して固化させるため、従来の製造方法では二
次加工を必要とした複雑形状の多孔質ガラスを、容易に
製造することができる。またゾル−ゲル法の特徴を活か
し、大型の製品についての割れ等の発生もなく均一な細
孔分布を持ち、且つ高強度の多孔質ガラス°ができる。
さらに、発泡剤の添加量及び焼結温度を調整することに
より、細孔径や細孔容積を調節することが可能になると
いう効果を有する。FIG. 1 is a process diagram showing the method for producing porous glass of the present invention. FIG. 2 is a process diagram showing a conventional method for manufacturing porous glass. [Effects of the Invention] As described above, according to the present invention, since the sol is injected into a mold of an arbitrary shape and solidified, a complex-shaped porous material that requires secondary processing in conventional manufacturing methods can be produced. Glass can be easily manufactured. Furthermore, by taking advantage of the characteristics of the sol-gel method, it is possible to produce porous glass with uniform pore distribution and high strength without the occurrence of cracks in large products. Furthermore, by adjusting the amount of foaming agent added and the sintering temperature, it is possible to adjust the pore diameter and pore volume.
Claims (1)
ルに発泡剤を添加し分散させた後、このゾルを望む形状
の型に注入し、固化・乾燥しドライゲルとし、このゲル
を発泡剤の分解温度以上に加熱し、含有している発泡剤
を分解させ、さらにこの混合物を焼結することを特徴と
する多孔質ガラスの製造方法。In the production of glass using the sol-gel method, a blowing agent is added to the created sol and dispersed, then this sol is poured into a mold of the desired shape, solidified and dried to form a dry gel, and this gel is heated to the decomposition temperature of the blowing agent. A method for producing porous glass, which comprises heating to the above temperature to decompose the foaming agent contained therein, and further sintering the mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17790288A JPH0226835A (en) | 1988-07-15 | 1988-07-15 | Method for manufacturing porous glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17790288A JPH0226835A (en) | 1988-07-15 | 1988-07-15 | Method for manufacturing porous glass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0226835A true JPH0226835A (en) | 1990-01-29 |
Family
ID=16039060
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17790288A Pending JPH0226835A (en) | 1988-07-15 | 1988-07-15 | Method for manufacturing porous glass |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0226835A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100430437B1 (en) * | 2000-05-16 | 2004-05-10 | 이상윤 | Method of producing foam glass for a fireproof insulating material |
| CN115321823A (en) * | 2022-09-21 | 2022-11-11 | 厦门市足来爽工贸有限公司 | Foam glass, preparation method and application thereof |
-
1988
- 1988-07-15 JP JP17790288A patent/JPH0226835A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100430437B1 (en) * | 2000-05-16 | 2004-05-10 | 이상윤 | Method of producing foam glass for a fireproof insulating material |
| CN115321823A (en) * | 2022-09-21 | 2022-11-11 | 厦门市足来爽工贸有限公司 | Foam glass, preparation method and application thereof |
| CN115321823B (en) * | 2022-09-21 | 2023-10-20 | 厦门市足来爽工贸有限公司 | Foam glass, preparation method and application thereof |
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