CA2246153C - Method for fabricating silica glass - Google Patents
Method for fabricating silica glass Download PDFInfo
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- CA2246153C CA2246153C CA002246153A CA2246153A CA2246153C CA 2246153 C CA2246153 C CA 2246153C CA 002246153 A CA002246153 A CA 002246153A CA 2246153 A CA2246153 A CA 2246153A CA 2246153 C CA2246153 C CA 2246153C
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- silica glass
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B20/00—Processes specially adapted for the production of quartz or fused silica articles, not otherwise provided for
-
- 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
- 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
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/06—Glass compositions containing silica with more than 90% silica by weight, e.g. quartz
-
- 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
- C03C2203/00—Production processes
- C03C2203/20—Wet processes, e.g. sol-gel process
- C03C2203/22—Wet processes, e.g. sol-gel process using colloidal silica sols
-
- 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
- C03C2203/00—Production processes
- C03C2203/20—Wet processes, e.g. sol-gel process
- C03C2203/30—Additives
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Glass Melting And Manufacturing (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Glass Compositions (AREA)
Abstract
A silica glass fabrication method. The method includes the steps of adding silica and a dispersant to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in a distilled water, and dispersing themixed solution, and adjusting the pH of the mixture, to form a sol; removing airbubbles from the sol, and then aging the sol; adding a polymerization initiator to the aging-treated sol, and adjusting the pH of the reaction mixture; pouring thereaction mixture into a mold, aging the mixture in an incubator at a high temperature and then gelating the resultant; aging the obtained gel, demolding the aging-treated gel, and then drying the demolded gel; thermally-treating the dried gel to remove organic substances from the gel; and performing a hydroxy group elimination reaction and a sintering reaction on the gel from which organic substances have been removed. Therefore, a high purity silica glass tube, in which cracking after drying scarcely occurs and shrinking ratio is markedly low, can be obtained. Also, a large silica glass tube can be manufactured by this fabrication method.
Description
CA 02246l~3 l998-08-28 METHOD FOR FABRICATING SILICA GLASS
BACKGROUND OF THE II~VENTION
1. Field of the Invention The present invention relates to a method for fabricating a silica glass fabrication method by a sol-gel process.
BACKGROUND OF THE II~VENTION
1. Field of the Invention The present invention relates to a method for fabricating a silica glass fabrication method by a sol-gel process.
2. Description of the Related Art In general, silica glass is transparent and chemically inert, and has high level of thermal stability and strength, and a low thermal expansion coefficient.
Because of such characteristics, the silica glass has been useful for an opticaldevice such as an optical fiber or optical lens.
Basically, the optical fiber is comprised of a core at the center thereof, and a cladding having a refractive index different from the core such that light is totally reflected from the core. In order to fabricate optical fibers, an optical fiber preform including a core rod and an overcladding tube enclosing the core rod is prepared.
Then, the optical fiber preform is thermally-treated and then extended to form the optical fibers.
The optical fiber preform is prepared by a modified chemical vapor deposition (MCVD), vapor phase axial deposition (VAD) or outside vapor deposition (OVD) method.
In the MCVD, the optical fiber preform is prepared from an overcladding tube made of high purity silica glass. Here, the silica glass overcladding tube is formed by a sol-gel process.
The sol-gel process, as a liquid phase process, can increase productivity and freely control composition of the product. Also, because the sol-gel process is performed at a low temperature, the sol-gel process is a very economical method.Also, since a high purity material is used as the starting material, this method is very useful for fabricating a photomask for a semiconductor and a high purity silica glass.
Hereinafter, a method of manufacturing an overcladding tube formed of silica glass by the sol-gel process will be briefly described.
CA 02246l~3 l998-08-28 First, silica particles are dispersed in water to form a sol. The formed sol is subjected to an aging treatment for a predetermined time. Then, the resultant sol is poured into a mold for gelation. After gelation is completed, the gel is separated from the mold and then dried.
Then, the dried gel is thermally-treated to remove organic substances from the gel. Then, a reaction for eliminating hydroxy groups from the gel from whichthe organic substances have been removed, and a sintering process are performed, thereby completing an overcladding tube made of silica glass.
Reactivity of the above-described sol-gel process depends on the gelation reaction temperature, composition of the sol, pH and solvent, and it is very difficult to maintain the reactivity within a favorable range by controlling such factors.Also, when drying the molded gel, many cracks are caused, and shrinking and cracking occur during sintering. In order to solve these problems, a method using a drying control chemical additive (DCCA) or a polymer binder, or redispersion method and supercritical drying method have been developed.
The method using the DCCA minimizes a local difference of solvent's evaporation rate from the gel, thereby minimizing the difference in the local stress of the samples during drying. As a result, the gel becomes hard, thereby decreasing generation of cracks.
According to the redispersion method, dried fine silica powder, i.e., fumed silica, is dispersed in water to form a sol, and then the sol is gelated. Duringgelation, the silica particles form an agglomerate due to hydrogen bonds. After drying the agglomerate, the dried agglomerate is subjected to a thermal process and grinding process and then redispersed in water. The redispersed product is gelated, molded, and then sintered.
However, the above methods are not effective in preventing cracking during the drying of the gel, and the preparing process is complicated.
SUMMARY OF THE INVENTION
To solve the above problems, it is an objective of the present invention to provide a method for fabricating a high density silica glass, in which cracking after drying process is suppressed and the cracking and shrinking after sintering process are reduced.
CA 02246l~3 l998-08-28 Accordingly, to achieve the above objective, there is provided a method for fabricating a silica glass comprising the steps of:
(a) adding silica and a dispersant to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in a distilled water, and dispersing the mixed solùtion, and adjusting the pH of the mixture, to form a sol;
(b) removing air bubbles from the sol, and then aging the sol;
~ ) adding a polymerization initiator to the aging-treated sol, and adjusting the pH of the reaction mixture;
(d) pouring the reaction mixture into a mold, aging the mixture in an incubator at a high temperature and then gelating the resultant;
(e) aging the obtained gel, demolding the aging-treated gel, and then drying the demolded gel;
(f) thermally-treating the dried gel to remove organic substances from the gel; and (g) performing a hydroxy group elimination reaction and a sintering reaction on the gel from which organic substances have been removed.
BRIEF DESCRIPTION OF THE DRAWING
The above objective and advantages of the present invention will become more apparent by describing in detail preferred embodiments thereof with reference to the attached drawing in which:
FIG. 1 is a flowchart illustrating a method for fabricating a silica glass according to the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
In a method for fabricating a silica glass according to the present invention, chemical gelation in which a silica is added to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in water, and dispersed and polymerized, and thermal gelation in which a gelling agent is added to a composition for silica glass and pH pf the resultant is properly adjusted, are simultaneously performed. As a result, a polymer binder having a 3-dimensional network structure, formed from the monomer for acrylic resin and the cross-linking CA 02246l~3 l998-08-28 agent, is evenly distributed in the whole gel, so that a conventional problem caused from the sol-gel process, that is, a density gradient, can be suppressed.Also, the strength of the gel increases, thereby suppressing cracking during drying and shortening the drying time.
Preferably, the content of the monomer for acrylic resin is 2~20wt% based on the weight of the premix solution, and the content of the cross-lining agent is 0.05~1.0wt% based on the weight of the premix solution.
Preferably, the concentration of the premix solution containing the monomer for acrylic resin and the cross-linking agent is low. If the concentration of the premix solution is low, carbon does not remain after organic substances are decomposed during the sol-gel process and the transparency of the silica glass is deteriorated after sintering process. Also, if such dilute premix solution is used, moist gel becomes smooth, and the strength of the moist gel can be improved through thermal gelation by controlling the pH.
The monomer for acrylic resin and the cross-linking agent are not specifically restricted. However, the monomer for acrylic resin is preferably acryl amide or methacryl amide, and the cross-linking agent is preferably N,N'-methylenebisacrylamide ((H2C=CHCONH)2CH2).
A method for fabricating a silica glass according to the present invention will be described with reference to FIG. 1.
First, a monomer for acrylic resin and a cross-linking agent are dissolved in deionized water to prepare a premix solution. A fumed silica and a dispersant are added to the premix solution, and then dispersed, and the pH of the reaction mixture is adjusted to 11~13, thereby forming a sol. Here, a mixing ratio of thefumed silica and the premix solution is 4:6~6:4 based on the weight. Here, the dispersant helps the fumed silica to be evenly dispersed in the premix solution.Any dispersant may be used without specific restriction. Preferably, however, tetramethylammonium hydroxide is preferably used as the dispersant.
Then, air bubbles are removed from the sol using a vacuum pump, and the sol is aged for a predetermined time to stabilize silica particles of the sol.
Then, a polymerization initiator and a catalyst are added to the reaction mixture, and a gelling agent is further added if required. Then, the pH of the reaction mixture is adjusted to 9~11. The obtained mixture is poured into a mold CA 02246l~3 l998-08-28 for gelation, and then left for aging in an incubator. Preferably, the aging process is performed at 60~100~C for 30 minutes~3 hours. Then, the gel is left for agingat room temperature.
Here, ammonium persulfate is used as the polymerization initiator, and methyl formate, methyl lactate or ethyl lactate is used as the gelling agent.
The aging-treated gel is demolded, and then dried in an incubator at 20~50~C and relative humidity (RH) of 70~95%. Then, in order to eliminate the organic substances remaining in the dried gel, such as additive and binder, a first thermally- treating process is performed. Here, for the first thermally- treating process, the gel is heated to 300~700~C at a rate of 50~C per hour, and then themaintained at that temperature for 2~8 hours. Also, in order to eliminate the remaining hydroxy groups from the first thermally-treated gel, the gel is heated to 900~1,200~C at a rate of 100~C per hour under a chlorine gas atmosphere, and then maintained at that temperature for 1~8 hours. Then, the gel is heated to 1,100~1,500~C at a rate of 100~C per hour under a helium gas atmosphere, and then maintained at that temperature for 1~8 hours. thereby completing a high density and high purity silica glass.
Examples of a method for fabricating silica glass according to the present invention will be described. However, the present invention is not limited to the following examples.
<Example 1>
4.8wt% of acryl amide and 0.2wt% of N,N'-methylenebisacrylamide were dissolved in 95.0wt% of deionized water to prepare a premix solution.
500ml of the premix solution, 500g of the fumed silica (Aerosil OX-50, Degussa Co.) and 52ml of trimethylammonium hydroxide (TMAH) aqueous solution (25.0wt% solution in water) were mixed and dispersed using a high shearmixer to prepare a sol. Then, air bubbles were removed from the sol using a vacuum pump, and aged for 10 hours. 8ml of ammonium persulfate aqueous solution (5.0wt% solution in water) as a polymerization initiator, and 8g of methyl formate (1.6wt% based on the weight of the silica) were added to and mixed with the aged sol.
CA 02246l~3 l998-08-28 The mixture was poured into a mold for gelation. Then, the mold containing the mixture was aged in an incubator at 70~C for 1 hour, and then gelated. The obtained moist gel was demolded, and dried in an incubator at 25~C and 75% RH
for 6 days. Then, the temperature of the gel was increased to 120~C at a rate of20~C per hour, and then maintained at that temperature for 5 hours to remove anyremaining moisture, thereby forming a dried gel.
Then, after heating the dried gel to 550~C at a rate of 50~C/hour, the dried gel was thermally-treated at that temperature for 5 hours to remove organic substances from the dried gel. The gel from which organic substances had been removed was heated to 1,000~C at a rate of 100~C/hour, and maintained at that temperature for 5 hours for glassification. Here, glassification was performed under a chlorine gas atmosphere to remove hydroxy groups.
Lastly, the resultant was heated to 1,400~C at a rate of 100~C/hour under a helium gas atmosphere, and the gel was sintered at that temperature for 4 hours,thereby forming a silica glass tube.
<Example 2>
A silica glass tube was manufactured by the same method as described in Example 1, except that methyl lactate was used instead of methyl formate.
<Example 3>
A silica glass tube was manufactured by the same method as described in Example 4, except that ethyl lactate was used instead of methyl formate.
<Example 4>
Because of such characteristics, the silica glass has been useful for an opticaldevice such as an optical fiber or optical lens.
Basically, the optical fiber is comprised of a core at the center thereof, and a cladding having a refractive index different from the core such that light is totally reflected from the core. In order to fabricate optical fibers, an optical fiber preform including a core rod and an overcladding tube enclosing the core rod is prepared.
Then, the optical fiber preform is thermally-treated and then extended to form the optical fibers.
The optical fiber preform is prepared by a modified chemical vapor deposition (MCVD), vapor phase axial deposition (VAD) or outside vapor deposition (OVD) method.
In the MCVD, the optical fiber preform is prepared from an overcladding tube made of high purity silica glass. Here, the silica glass overcladding tube is formed by a sol-gel process.
The sol-gel process, as a liquid phase process, can increase productivity and freely control composition of the product. Also, because the sol-gel process is performed at a low temperature, the sol-gel process is a very economical method.Also, since a high purity material is used as the starting material, this method is very useful for fabricating a photomask for a semiconductor and a high purity silica glass.
Hereinafter, a method of manufacturing an overcladding tube formed of silica glass by the sol-gel process will be briefly described.
CA 02246l~3 l998-08-28 First, silica particles are dispersed in water to form a sol. The formed sol is subjected to an aging treatment for a predetermined time. Then, the resultant sol is poured into a mold for gelation. After gelation is completed, the gel is separated from the mold and then dried.
Then, the dried gel is thermally-treated to remove organic substances from the gel. Then, a reaction for eliminating hydroxy groups from the gel from whichthe organic substances have been removed, and a sintering process are performed, thereby completing an overcladding tube made of silica glass.
Reactivity of the above-described sol-gel process depends on the gelation reaction temperature, composition of the sol, pH and solvent, and it is very difficult to maintain the reactivity within a favorable range by controlling such factors.Also, when drying the molded gel, many cracks are caused, and shrinking and cracking occur during sintering. In order to solve these problems, a method using a drying control chemical additive (DCCA) or a polymer binder, or redispersion method and supercritical drying method have been developed.
The method using the DCCA minimizes a local difference of solvent's evaporation rate from the gel, thereby minimizing the difference in the local stress of the samples during drying. As a result, the gel becomes hard, thereby decreasing generation of cracks.
According to the redispersion method, dried fine silica powder, i.e., fumed silica, is dispersed in water to form a sol, and then the sol is gelated. Duringgelation, the silica particles form an agglomerate due to hydrogen bonds. After drying the agglomerate, the dried agglomerate is subjected to a thermal process and grinding process and then redispersed in water. The redispersed product is gelated, molded, and then sintered.
However, the above methods are not effective in preventing cracking during the drying of the gel, and the preparing process is complicated.
SUMMARY OF THE INVENTION
To solve the above problems, it is an objective of the present invention to provide a method for fabricating a high density silica glass, in which cracking after drying process is suppressed and the cracking and shrinking after sintering process are reduced.
CA 02246l~3 l998-08-28 Accordingly, to achieve the above objective, there is provided a method for fabricating a silica glass comprising the steps of:
(a) adding silica and a dispersant to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in a distilled water, and dispersing the mixed solùtion, and adjusting the pH of the mixture, to form a sol;
(b) removing air bubbles from the sol, and then aging the sol;
~ ) adding a polymerization initiator to the aging-treated sol, and adjusting the pH of the reaction mixture;
(d) pouring the reaction mixture into a mold, aging the mixture in an incubator at a high temperature and then gelating the resultant;
(e) aging the obtained gel, demolding the aging-treated gel, and then drying the demolded gel;
(f) thermally-treating the dried gel to remove organic substances from the gel; and (g) performing a hydroxy group elimination reaction and a sintering reaction on the gel from which organic substances have been removed.
BRIEF DESCRIPTION OF THE DRAWING
The above objective and advantages of the present invention will become more apparent by describing in detail preferred embodiments thereof with reference to the attached drawing in which:
FIG. 1 is a flowchart illustrating a method for fabricating a silica glass according to the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
In a method for fabricating a silica glass according to the present invention, chemical gelation in which a silica is added to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in water, and dispersed and polymerized, and thermal gelation in which a gelling agent is added to a composition for silica glass and pH pf the resultant is properly adjusted, are simultaneously performed. As a result, a polymer binder having a 3-dimensional network structure, formed from the monomer for acrylic resin and the cross-linking CA 02246l~3 l998-08-28 agent, is evenly distributed in the whole gel, so that a conventional problem caused from the sol-gel process, that is, a density gradient, can be suppressed.Also, the strength of the gel increases, thereby suppressing cracking during drying and shortening the drying time.
Preferably, the content of the monomer for acrylic resin is 2~20wt% based on the weight of the premix solution, and the content of the cross-lining agent is 0.05~1.0wt% based on the weight of the premix solution.
Preferably, the concentration of the premix solution containing the monomer for acrylic resin and the cross-linking agent is low. If the concentration of the premix solution is low, carbon does not remain after organic substances are decomposed during the sol-gel process and the transparency of the silica glass is deteriorated after sintering process. Also, if such dilute premix solution is used, moist gel becomes smooth, and the strength of the moist gel can be improved through thermal gelation by controlling the pH.
The monomer for acrylic resin and the cross-linking agent are not specifically restricted. However, the monomer for acrylic resin is preferably acryl amide or methacryl amide, and the cross-linking agent is preferably N,N'-methylenebisacrylamide ((H2C=CHCONH)2CH2).
A method for fabricating a silica glass according to the present invention will be described with reference to FIG. 1.
First, a monomer for acrylic resin and a cross-linking agent are dissolved in deionized water to prepare a premix solution. A fumed silica and a dispersant are added to the premix solution, and then dispersed, and the pH of the reaction mixture is adjusted to 11~13, thereby forming a sol. Here, a mixing ratio of thefumed silica and the premix solution is 4:6~6:4 based on the weight. Here, the dispersant helps the fumed silica to be evenly dispersed in the premix solution.Any dispersant may be used without specific restriction. Preferably, however, tetramethylammonium hydroxide is preferably used as the dispersant.
Then, air bubbles are removed from the sol using a vacuum pump, and the sol is aged for a predetermined time to stabilize silica particles of the sol.
Then, a polymerization initiator and a catalyst are added to the reaction mixture, and a gelling agent is further added if required. Then, the pH of the reaction mixture is adjusted to 9~11. The obtained mixture is poured into a mold CA 02246l~3 l998-08-28 for gelation, and then left for aging in an incubator. Preferably, the aging process is performed at 60~100~C for 30 minutes~3 hours. Then, the gel is left for agingat room temperature.
Here, ammonium persulfate is used as the polymerization initiator, and methyl formate, methyl lactate or ethyl lactate is used as the gelling agent.
The aging-treated gel is demolded, and then dried in an incubator at 20~50~C and relative humidity (RH) of 70~95%. Then, in order to eliminate the organic substances remaining in the dried gel, such as additive and binder, a first thermally- treating process is performed. Here, for the first thermally- treating process, the gel is heated to 300~700~C at a rate of 50~C per hour, and then themaintained at that temperature for 2~8 hours. Also, in order to eliminate the remaining hydroxy groups from the first thermally-treated gel, the gel is heated to 900~1,200~C at a rate of 100~C per hour under a chlorine gas atmosphere, and then maintained at that temperature for 1~8 hours. Then, the gel is heated to 1,100~1,500~C at a rate of 100~C per hour under a helium gas atmosphere, and then maintained at that temperature for 1~8 hours. thereby completing a high density and high purity silica glass.
Examples of a method for fabricating silica glass according to the present invention will be described. However, the present invention is not limited to the following examples.
<Example 1>
4.8wt% of acryl amide and 0.2wt% of N,N'-methylenebisacrylamide were dissolved in 95.0wt% of deionized water to prepare a premix solution.
500ml of the premix solution, 500g of the fumed silica (Aerosil OX-50, Degussa Co.) and 52ml of trimethylammonium hydroxide (TMAH) aqueous solution (25.0wt% solution in water) were mixed and dispersed using a high shearmixer to prepare a sol. Then, air bubbles were removed from the sol using a vacuum pump, and aged for 10 hours. 8ml of ammonium persulfate aqueous solution (5.0wt% solution in water) as a polymerization initiator, and 8g of methyl formate (1.6wt% based on the weight of the silica) were added to and mixed with the aged sol.
CA 02246l~3 l998-08-28 The mixture was poured into a mold for gelation. Then, the mold containing the mixture was aged in an incubator at 70~C for 1 hour, and then gelated. The obtained moist gel was demolded, and dried in an incubator at 25~C and 75% RH
for 6 days. Then, the temperature of the gel was increased to 120~C at a rate of20~C per hour, and then maintained at that temperature for 5 hours to remove anyremaining moisture, thereby forming a dried gel.
Then, after heating the dried gel to 550~C at a rate of 50~C/hour, the dried gel was thermally-treated at that temperature for 5 hours to remove organic substances from the dried gel. The gel from which organic substances had been removed was heated to 1,000~C at a rate of 100~C/hour, and maintained at that temperature for 5 hours for glassification. Here, glassification was performed under a chlorine gas atmosphere to remove hydroxy groups.
Lastly, the resultant was heated to 1,400~C at a rate of 100~C/hour under a helium gas atmosphere, and the gel was sintered at that temperature for 4 hours,thereby forming a silica glass tube.
<Example 2>
A silica glass tube was manufactured by the same method as described in Example 1, except that methyl lactate was used instead of methyl formate.
<Example 3>
A silica glass tube was manufactured by the same method as described in Example 4, except that ethyl lactate was used instead of methyl formate.
<Example 4>
3.9wt% of methacryl amide, 0.16wt% of N,N'-methylenebisacrylamide were dissolved in 95.94wt% of deionized water to prepare a premix solution.
500ml of the premix solution, 500g of the fumed silica (Aerosil OX-50, Degussa Co.) and 52ml of TMAH aqueous solution (25.0wt% solution in water) were mixed and dispersed using a high shear mixer to prepare a sol.
Then, air bubbles were removed from the sol using a vacuum pump, and aged for 10 hours. 8ml of ammonium persulfate aqueous solution (5.0wt%
solution in water) was added to the aged sol, and the air bubbles were removed CA 02246l~3 l998-08-28 from the reaction mixture. Then, 8g of methyl formate (1.6wt% based on the weight of silica) was added to and mixed with the reaction mixture. Then, the obtained mixture was poured into a mold, aged in an incubator at 70~C for 1 hour, and then gelated into an intended shape.
Aftèr demolding the obtained moist gel, and dried in an incubator at 30~C
and 90% RH for 10 days. Then, the resultant was heated to 700~C at a rate of 50~C per hour, and then maintained at that temperature for 4 hours. Then, after heating the dried gel to 1,100~C at a rate of 100~C/hour, the dried gel was thermally-treated at 1,100~C for 5 hours. Here, the thermally-treating process was performed under a chlorine gas atmosphere to remove the remaining hydroxy groups.
Lastly, the resultant was heated to 1,500~C at a rate of 100~C/hour under a helium gas atmosphere, and the gel was sintered at that temperature for 5 hours,thereby forming a silica glass tube.
Strength of the gels manufactured by Examples 1 through 4 was measured.
According to the result, strength of the gel was found to be increased compared with the conventional case, so it is easy to handle the gel.
Also, it was observed whether cracks and shrinking of the silica glass tubes manufactured by Examples 1 through 4 were generated.
As a result, in the silica glass tubes manufactured as in Examples 1 and 4, cracking after drying process and shrinking were both decreased.
In the method for fabricating a silica glass according to the present invention, a high purity silica glass tube, in which cracking after drying scarcely occurs and shrinking ratio is markedly low, can be obtained. Also, a large silica glass tube can be manufactured by this fabrication method.
The silica glass obtained by the fabrication method according to the present invention can be applied to a silica glass for semiconductor devices, an opticallens and so on as well as for a optical fiber preform.
500ml of the premix solution, 500g of the fumed silica (Aerosil OX-50, Degussa Co.) and 52ml of TMAH aqueous solution (25.0wt% solution in water) were mixed and dispersed using a high shear mixer to prepare a sol.
Then, air bubbles were removed from the sol using a vacuum pump, and aged for 10 hours. 8ml of ammonium persulfate aqueous solution (5.0wt%
solution in water) was added to the aged sol, and the air bubbles were removed CA 02246l~3 l998-08-28 from the reaction mixture. Then, 8g of methyl formate (1.6wt% based on the weight of silica) was added to and mixed with the reaction mixture. Then, the obtained mixture was poured into a mold, aged in an incubator at 70~C for 1 hour, and then gelated into an intended shape.
Aftèr demolding the obtained moist gel, and dried in an incubator at 30~C
and 90% RH for 10 days. Then, the resultant was heated to 700~C at a rate of 50~C per hour, and then maintained at that temperature for 4 hours. Then, after heating the dried gel to 1,100~C at a rate of 100~C/hour, the dried gel was thermally-treated at 1,100~C for 5 hours. Here, the thermally-treating process was performed under a chlorine gas atmosphere to remove the remaining hydroxy groups.
Lastly, the resultant was heated to 1,500~C at a rate of 100~C/hour under a helium gas atmosphere, and the gel was sintered at that temperature for 5 hours,thereby forming a silica glass tube.
Strength of the gels manufactured by Examples 1 through 4 was measured.
According to the result, strength of the gel was found to be increased compared with the conventional case, so it is easy to handle the gel.
Also, it was observed whether cracks and shrinking of the silica glass tubes manufactured by Examples 1 through 4 were generated.
As a result, in the silica glass tubes manufactured as in Examples 1 and 4, cracking after drying process and shrinking were both decreased.
In the method for fabricating a silica glass according to the present invention, a high purity silica glass tube, in which cracking after drying scarcely occurs and shrinking ratio is markedly low, can be obtained. Also, a large silica glass tube can be manufactured by this fabrication method.
The silica glass obtained by the fabrication method according to the present invention can be applied to a silica glass for semiconductor devices, an opticallens and so on as well as for a optical fiber preform.
Claims (9)
1. A method for fabricating a silica glass comprising the steps of:
(a) adding silica and a dispersant to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in a distilled water, and dispersing the mixed solution, and adjusting the pH of the mixture, to form a sol;
(b) removing air bubbles from the sol, and then aging the sol;
(c) adding a polymerization initiator to the aging-treated sol, and adjusting the pH of the reaction mixture;
(d) pouring the reaction mixture into a mold, aging the mixture in an incubator at a high temperature and then gelating the resultant;
(e) aging the obtained gel, demolding the aging-treated gel, and then drying the demolded gel;
(f) thermally-treating the dried gel to remove organic substances from the gel; and (g) performing a hydroxy group elimination reaction and a sintering reaction on the gel from which organic substances have been removed.
(a) adding silica and a dispersant to a premix solution obtained by dissolving a monomer for acrylic resin and a cross-linking agent in a distilled water, and dispersing the mixed solution, and adjusting the pH of the mixture, to form a sol;
(b) removing air bubbles from the sol, and then aging the sol;
(c) adding a polymerization initiator to the aging-treated sol, and adjusting the pH of the reaction mixture;
(d) pouring the reaction mixture into a mold, aging the mixture in an incubator at a high temperature and then gelating the resultant;
(e) aging the obtained gel, demolding the aging-treated gel, and then drying the demolded gel;
(f) thermally-treating the dried gel to remove organic substances from the gel; and (g) performing a hydroxy group elimination reaction and a sintering reaction on the gel from which organic substances have been removed.
2. The method of claim 1, wherein in the step (c) a gelling agent is further added in addition to the polymerization initiator.
3. The method of claim 2, wherein the gelling agent is at least one selected from the group consisting of methyl formate, methyl lactate and ethyl lactate.
4. The method of claim 1, wherein the aging in the incubator of the step (d) is performed at 60-100°C.
5. The method of claim 1, wherein the content of the monomer for acrylic resin is 2-20wt% based on the weight of the premix solution.
6. The method of claim 1, wherein the content of the cross-linking agent is 0.05-1.0wt% based on the weight of the premix solution.
7. The method of claim 1, wherein the monomer for acrylic resin is one selected from the group consisting of acryl amide or methacryl amide, and the cross-linking agent is N,N'-methylenebisacrylamide.
8. The method of claim 1, wherein the mixing ratio of the silica and the premix solution is 4:6-6:4 based on the weight.
9. The method of claim 1, wherein the polymerization initiator is ammonium persulfate.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR19970042751 | 1997-08-29 | ||
| KR97-42751 | 1997-08-29 | ||
| KR1019980019263A KR100252185B1 (en) | 1997-08-29 | 1998-05-27 | Method of manufacturing silica glass |
| KR98-19263 | 1998-05-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2246153A1 CA2246153A1 (en) | 1999-02-28 |
| CA2246153C true CA2246153C (en) | 2001-11-27 |
Family
ID=26633040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002246153A Expired - Fee Related CA2246153C (en) | 1997-08-29 | 1998-08-28 | Method for fabricating silica glass |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JP2938058B2 (en) |
| KR (1) | KR100252185B1 (en) |
| CN (1) | CN1115308C (en) |
| CA (1) | CA2246153C (en) |
| FR (1) | FR2767808B1 (en) |
| GB (1) | GB2328685B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100322132B1 (en) * | 1999-01-29 | 2002-01-29 | 윤종용 | Silica glass composition for sol-gel process |
| KR20000074724A (en) * | 1999-05-25 | 2000-12-15 | 윤종용 | Manufacturing method of silica glass for sol-gel process |
| CN1107657C (en) * | 2000-04-17 | 2003-05-07 | 袁茂豪 | Production process of high-silicon quartzite powder |
| KR20050080879A (en) * | 2004-02-11 | 2005-08-18 | 삼성전자주식회사 | Method for fabricating holey fiber preform |
| EP3266752B1 (en) * | 2015-03-04 | 2024-07-10 | Kyushu University National University Corporation | Silica glass precursor production method, silica glass precursor, silica glass production method |
| DE102016012003A1 (en) * | 2016-10-06 | 2018-04-12 | Karlsruher Institut für Technologie | Composition and method for producing a shaped body from high-purity, transparent quartz glass by means of additive manufacturing |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2113200B (en) * | 1982-01-08 | 1985-06-19 | Hitachi Ltd | Process for producing optical glass |
| JP2635313B2 (en) * | 1986-05-14 | 1997-07-30 | 日立化成工業株式会社 | Method for producing silica glass |
| JPS6385018A (en) * | 1986-09-26 | 1988-04-15 | Harima Ceramic Co Ltd | Production of high purity silica glass |
| JPH01176235A (en) * | 1987-12-29 | 1989-07-12 | Hitachi Chem Co Ltd | Production of silica glass |
| JPH01176234A (en) * | 1987-12-29 | 1989-07-12 | Hitachi Chem Co Ltd | Production of silicate glass |
| US4894194A (en) * | 1988-02-22 | 1990-01-16 | Martin Marietta Energy Systems, Inc. | Method for molding ceramic powders |
| DE4130440A1 (en) * | 1991-09-13 | 1993-03-18 | Philips Patentverwaltung | METHOD FOR PRODUCING MOLDED BODIES FROM CERAMIC OR GLASS |
| FR2681534B1 (en) * | 1991-09-20 | 1995-01-27 | Rhone Poulenc Chimie | CONCENTRATED COLLOUIDAL SOLUTIONS OF NON-AGGREGATED MONOCRYSTALLINE PARTICLES OF METAL OXIDES, THEIR PREPARATION PROCESS AND THEIR APPLICATION FOR OBTAINING FILMS. |
| US5240488A (en) * | 1992-08-14 | 1993-08-31 | At&T Bell Laboratories | Manufacture of vitreous silica product via a sol-gel process using a polymer additive |
-
1998
- 1998-05-27 KR KR1019980019263A patent/KR100252185B1/en not_active Expired - Fee Related
- 1998-08-20 JP JP10234619A patent/JP2938058B2/en not_active Expired - Fee Related
- 1998-08-20 GB GB9818056A patent/GB2328685B/en not_active Expired - Fee Related
- 1998-08-28 FR FR9810826A patent/FR2767808B1/en not_active Expired - Fee Related
- 1998-08-28 CN CN98117652A patent/CN1115308C/en not_active Expired - Fee Related
- 1998-08-28 CA CA002246153A patent/CA2246153C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| KR19990023144A (en) | 1999-03-25 |
| KR100252185B1 (en) | 2000-04-15 |
| JPH11147727A (en) | 1999-06-02 |
| CN1210825A (en) | 1999-03-17 |
| FR2767808A1 (en) | 1999-03-05 |
| CA2246153A1 (en) | 1999-02-28 |
| GB2328685A (en) | 1999-03-03 |
| CN1115308C (en) | 2003-07-23 |
| JP2938058B2 (en) | 1999-08-23 |
| FR2767808B1 (en) | 2000-12-15 |
| GB9818056D0 (en) | 1998-10-14 |
| GB2328685B (en) | 1999-09-29 |
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