WO1997030933A1 - Pure fused silica, furnace and method - Google Patents

Pure fused silica, furnace and method Download PDF

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Publication number
WO1997030933A1
WO1997030933A1 PCT/US1997/001681 US9701681W WO9730933A1 WO 1997030933 A1 WO1997030933 A1 WO 1997030933A1 US 9701681 W US9701681 W US 9701681W WO 9730933 A1 WO9730933 A1 WO 9730933A1
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WO
WIPO (PCT)
Prior art keywords
refractory
accordance
fumace
halogen
fused silica
Prior art date
Application number
PCT/US1997/001681
Other languages
French (fr)
Inventor
Robert S. Pavlik, Jr.
Daniel R. Sempolinski
Michael H. Wasilewski
Original Assignee
Corning Incorporated
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 Corning Incorporated filed Critical Corning Incorporated
Priority to EP97905726A priority Critical patent/EP0881987A4/en
Priority to US09/117,980 priority patent/US6096761A/en
Priority to US09/125,208 priority patent/US6174509B1/en
Priority to JP9530179A priority patent/JP2000505036A/en
Publication of WO1997030933A1 publication Critical patent/WO1997030933A1/en

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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
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/06Glass compositions containing silica with more than 90% silica by weight, e.g. quartz
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/14Other methods of shaping glass by gas- or vapour- phase reaction processes
    • C03B19/1407Deposition reactors therefor
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/14Other methods of shaping glass by gas- or vapour- phase reaction processes
    • C03B19/1484Means for supporting, rotating or translating the article being formed
    • C03B19/1492Deposition substrates, e.g. targets
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/53After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone involving the removal of at least part of the materials of the treated article, e.g. etching, drying of hardened concrete
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2201/00Type of glass produced
    • C03B2201/02Pure silica glass, e.g. pure fused quartz
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2201/00Type of glass produced
    • C03B2201/02Pure silica glass, e.g. pure fused quartz
    • C03B2201/03Impurity concentration specified
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/50Multiple burner arrangements
    • C03B2207/52Linear array of like burners
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/50Multiple burner arrangements
    • C03B2207/54Multiple burner arrangements combined with means for heating the deposit, e.g. non-deposition burner

Definitions

  • An article of relatively pure fused silica and a furnace and method for producing the article.
  • Relatively pure metal oxides are produced by thermal decomposition of precursors and deposition ofthe resulting oxides.
  • the precursor may take the form of a vapor, or may be carried by a vapor. It may be decomposed by either flame hydrolysis or pyrolysis.
  • One such process is production of fused silica by hydrolysis or pyrolysis of silicon tetrachloride.
  • Early patents disclosing such processes for producing silica are United States Patent No. 2,239,551 (Nordberg) and 2,272,342 (Hyde).
  • a commercial application of flame hydrolysis involves forming and depositing particles of fused silica to form large bodies (boules). Such boules may be used individually, or may be finished and integrated together into large optical bodies, such as telescope mirrors.
  • SiCl 4 is hydrolyzed, and the hydrolyzed vapor is passed into a flame to form molten particles of fused silica.
  • the particles are continuously deposited on a bait, or in a crucible, known as a cup, to form a boule.
  • these measures constituted providing a purer zircon refractory for use in constructing a furnace in which the fused silica was deposited to form a boule.
  • dispersants, binders and water relatively free of sodium ions in producing zircon refractory components for the fumace.
  • UV wavelength radiation from an excimer type laser This laser emits radiation at about 193 nm and 248 nm wavelengths.
  • One aspect ofthe present invention resides in an improved method of producing a fused silica body by introducing a silicon-containing compound into a flame to form molten silica particles and collecting those particles in the form of a fused silica body in a fumace constructed of refractory materials, the improvement comprising constructing at least a portion ofthe furnace from refractory materials that have been exposed to a reactive, halogen-containing gas to react with and thereby cleanse the refractory of contaminating metals.
  • a further aspect ofthe invention resides in a relatively pure fused silica material in which the fused silica has a transmittance value of at least 99.5% for 248 nm radiation, a transmittance value of at least 98% for 193 nm radiation, at least a substantial portion of the body has an acceptable fluorescence level when exposed to such radiation, and the fused silica material has a content of contaminating metal ions less than 100 ppb.
  • the invention further resides in a refractory fumace for collecting molten silica particles in the form of a solid body, at least a portion ofthe fumace being constructed of a refractory that contains metal contaminants in an amount less than 300 ppm.
  • FIGURE in the accompanying drawing is a schematic representation of an apparatus and process for depositing a large body of fused silica.
  • the conventional boule process used in making fused silica is a one-step process.
  • a carrier gas is bubbled through a SiCl 4 feedstock that is maintained at a specified low temperature.
  • the vaporous SiCl 4 is entrained in the carrier gas and is thereby transported to the reaction site.
  • the reaction site is comprised of a number of burners that combust and oxidize the vaporous SiCl 4 to deposit silica at a temperature greater than 1600° C.
  • the apparatus and transfer system be capable of vaporizing the feedstock and delivering the vaporized feedstock to a burner in the vapor state.
  • the apparatus and process may remain substantially unchanged with one major exception.
  • the SiCl 4 feedstock is replaced by a polymethylsiloxane.
  • Use of this substitute feedstock may require some minor adjustments, such as a somewhat higher delivery temperature (e.g., 100-150° C). This is due to the siloxane having a somewhat lower vapor pressure than SiCl 4 .
  • FIGURE 1 in the accompanying drawing is a schematic representation of an apparatus and process for producing and depositing molten silica particles to build up a large, fused silica boule.
  • the apparatus generally designated by the numeral 10, includes a feedstock source 12. Nitrogen, or a nitrogen/oxygen mixture, is used as the carrier gas.
  • a bypass stream of nitrogen 14 is introduced to prevent saturation ofthe vaporous stream.
  • the vaporous reactant is passed through a distribution mechamsm to the reaction site wherein a number of burners 18 are present in close proximity to a furnace crown 20.
  • the reactant is combined with a fuel oxygen mixture 22 at these burners, and is combusted and oxidized to deposit silica at a temperature greater than 1 00° C.
  • High purity metal oxide soot and heat are directed downwardly through the refractory fumace crown 20.
  • the silica is immediately deposited and consolidated to a non-porous mass 24 on hot cup 26.
  • Contaminating metals can be present in the raw materials employed in production of fumace refractories.
  • the metals may also be entrained during sintering ofthe refractory, or during any subsequent operations, such as sawing or grinding.
  • Zircon is a relatively clean refractory, particularly when prepared as described in the Sempoiinski et al. patents.
  • the superior transmission properties required for such demanding uses as microlithography applications require control of all metal contaminants at a level below 100 parts per billion (ppb).
  • this degree of contaminating metal control in a collection fumace can be achieved by constructing the furnace of refractory materials containing less than 300 parts per million (ppm) ofthe contaminating metals.
  • ppm parts per million
  • zircon refractories used in a collection furnace for fused silica deposition This desirable end is accomplished, in accordance with the present invention, by firing the fumace refractories in a halogen-containing atmosphere. The halogen reacts with and removes the contaminating metals from at least the exposed surface ofthe refractory.
  • the cleansing gas can be used in essentially pure form. However, we have found it convenient, and effective, to employ as little as 5% ofthe cleansing gas in an inert gas, such as helium or argon, with a somewhat longer treatment time.
  • the cleansing treatment may employ a continuous flow ofthe halogen gas. Alternatively, a pulsed type treatment may be used wherein gas is repeatedly introduced into the firing chamber and subsequently exhausted.
  • the cleansing action can occur at a temperature as low as 700°C. However, it is usually preferred to employ somewhat higher temperatures in the range of 1100 to 1500°C. Above 1500°C, zircon starts to thermally dissociate, thereby resulting in a weaker refractory body.
  • the invention is here described with reference to treatment of zircon refractory fumace elements. However, it will be appreciated that it is also applicable to cleansing contaminating metals from other types of refractory articles.
  • the cleansing process on a refractory body may be carried out either prior to assembly into a fumace or after assembly.
  • the treatment may also be carried out during production ofthe refractory.
  • High temperature refractories, such as zircon are sintered in air at temperatures in excess of 1500°C. As the sintered furnace components are being cooled, the cooling step can be interrupted at an appropriate temperature, for example, 1200°C.
  • the sintering fumace is then switched to a halogen-containing atmosphere, and the temperature maintained for the necessary time to cleanse the refractory ofthe contaminating metals.
  • the use of refractories chemically cleaned in accordance with the invention provides several advantages.
  • the cleaner deposition fumace provides a fused silica product of high purity. It provides high, consistent yields of fused silica glass having an acceptably high transmission of short wavelength UV radiation and a low level of fluorescence. Further, the glass is less prone to increases in radiation damage and fluorescence in service. These desired ends are achieved without requiring change in, or compromise of, either the fumace design or the silica forming and deposition process.
  • the effectiveness ofthe cleansing treatment was demonstrated by comparing two sets of fused silica test pieces. One set was taken from boules deposited in an untreated collection fumace. A second set was taken from boules deposited in a treated fumace.
  • the fiirnaces were constructed in essentially identical design with sintered zircon refractory crowns and cup liners.
  • the refractories in the treated fumace were soaked for eight hours in a furnace operating at 1300°C. A flowing atmosphere of 5.7% Cl 2 and
  • the fused silica boules described above were also analyzed to determine the percentage of boule depth that exhibited an acceptable low level of fluorescence.
  • Fluorescence is determined by integrating the intensities measured over the range of 400- 700 nm. To be acceptable, a glass test piece must exhibit a value, as so determined, that is below 4.2x10' 9 watts/cm 2 when the glass is exposed to an emitting laser operating at 15 mj/cm 2 and 200 Hz. Glass from the untreated fumace was completely unacceptable. There was no portion ofthe boule in which the fluorescence value was acceptably low. Glass from the treated fumace had acceptable glass to a depth of 3.53 inches. This represented 59.3% of the total depth.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Ceramic Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Structural Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Glass Compositions (AREA)

Abstract

An article of relatively pure silica, and a furnace and method of producing the article. The article is produced by collecting molten silica particles (24) in a refractory furnace in which at least a portion of the refractory has been exposed to a halogen-containing gas to react with contaminating metal ions in the refractory.

Description

PURE FUSED SILICA, FURNACE AND METHOD
This application claims the benefit of U.S. Provisional Application No. 60/011997, express mailed February 21, 1996, entitled PURE FUSED SILICA, FURNACE AND METHOD, by Robert S. Pavlik, Jr., Daniel R. Sempolinski and Michael R. Wasilewski.
FIELD OF THE INVENTION
An article of relatively pure fused silica, and a furnace and method for producing the article.
BACKGROUND OF THE INVENTION
Relatively pure metal oxides are produced by thermal decomposition of precursors and deposition ofthe resulting oxides. The precursor may take the form of a vapor, or may be carried by a vapor. It may be decomposed by either flame hydrolysis or pyrolysis. One such process is production of fused silica by hydrolysis or pyrolysis of silicon tetrachloride. Early patents disclosing such processes for producing silica are United States Patent No. 2,239,551 (Nordberg) and 2,272,342 (Hyde). A commercial application of flame hydrolysis involves forming and depositing particles of fused silica to form large bodies (boules). Such boules may be used individually, or may be finished and integrated together into large optical bodies, such as telescope mirrors. In this procedure, SiCl4 is hydrolyzed, and the hydrolyzed vapor is passed into a flame to form molten particles of fused silica. The particles are continuously deposited on a bait, or in a crucible, known as a cup, to form a boule.
A serious drawback in this process has been the need to dispose ofthe HCl by¬ product in an environmentally safe manner. Accordingly, it has been proposed, in United States Patent No. 5,043,002 (Dobbins et al ), to employ a halide-free, silicon-containing compound as a substitute for SiCl4. In particular, the patent proposes using a polymethylsiloxane, such as octamethylcyclotetrasiloxane, to provide the vaporous reactant for the hydrolysis or pyrolysis process.
In order to introduce a substitute precursor, it is, of course, critically necessary to avoid any significant change in the properties ofthe fused silica product. Unfortunately, the substitution proposed by the Dobbins et al. patent did lead to significant property changes. One such change was a reduction in UV transmission properties. Another was development of fluorescence in the glass that increased when the glass was exposed to short wavelength radiation. Studies revealed that a factor in the transmission loss was sodium ion content in the glass. United States Patent Nos. 5,332,702 and 5,395,413 (Sempoiinski et al.) describe remedial measures taken to reduce the sodium ion content. Essentially, these measures constituted providing a purer zircon refractory for use in constructing a furnace in which the fused silica was deposited to form a boule. In particular, it was found necessary to use dispersants, binders and water relatively free of sodium ions in producing zircon refractory components for the fumace.
An improved product was obtained by adopting the practices prescribed in the Sempoiinski et al. patents. However, use ofthe fused silica in certain applications made it apparent that further improvements were necessary to meet the critical requirements of these applications. One such application is lenses designed for transmission of very short
UV wavelength radiation from an excimer type laser. This laser emits radiation at about 193 nm and 248 nm wavelengths.
It was found that lenses produced from available fused silica did not provide acceptable transmission ofthe short wavelength radiation and exhibited an undesirable fluorescence. Both ofthese conditions tend to become worse with service time. The loss of transmission, or darkening ofthe glass, is commonly referred to as UV absoφtion damage.
It is a primary purpose ofthe present invention to provide a fused silica material that alleviates these problems. Another purpose is to provide an improved fused silica glass for lenses used with lasers, especially for microlithographic work. A further purpose is to provide an improved fumace for collection ofthe fused silica in the form of a boule. A still further purpose is to provide a method of achieving the improved collecting fumace and glass produced therein.
SUMMARY OF THE INVENTION
One aspect ofthe present invention resides in an improved method of producing a fused silica body by introducing a silicon-containing compound into a flame to form molten silica particles and collecting those particles in the form of a fused silica body in a fumace constructed of refractory materials, the improvement comprising constructing at least a portion ofthe furnace from refractory materials that have been exposed to a reactive, halogen-containing gas to react with and thereby cleanse the refractory of contaminating metals.
A further aspect ofthe invention resides in a relatively pure fused silica material in which the fused silica has a transmittance value of at least 99.5% for 248 nm radiation, a transmittance value of at least 98% for 193 nm radiation, at least a substantial portion of the body has an acceptable fluorescence level when exposed to such radiation, and the fused silica material has a content of contaminating metal ions less than 100 ppb.
The invention further resides in a refractory fumace for collecting molten silica particles in the form of a solid body, at least a portion ofthe fumace being constructed of a refractory that contains metal contaminants in an amount less than 300 ppm.
BRIEF DESCRIPTION OF THE DRAWINGS
The single FIGURE in the accompanying drawing is a schematic representation of an apparatus and process for depositing a large body of fused silica. PRIQR ART
Literature deemed of possible interest is listed in an accompanying document.
DESCRIPTION OF THE INVENTION
The conventional boule process used in making fused silica is a one-step process. In this process, a carrier gas is bubbled through a SiCl4 feedstock that is maintained at a specified low temperature. The vaporous SiCl4 is entrained in the carrier gas and is thereby transported to the reaction site. The reaction site is comprised of a number of burners that combust and oxidize the vaporous SiCl4 to deposit silica at a temperature greater than 1600° C.
The principal requirements in the conventional process are that the apparatus and transfer system be capable of vaporizing the feedstock and delivering the vaporized feedstock to a burner in the vapor state. As described in the Dobbins et al. patent, the apparatus and process may remain substantially unchanged with one major exception. The SiCl4 feedstock is replaced by a polymethylsiloxane. Use of this substitute feedstock may require some minor adjustments, such as a somewhat higher delivery temperature (e.g., 100-150° C). This is due to the siloxane having a somewhat lower vapor pressure than SiCl4.
FIGURE 1 in the accompanying drawing is a schematic representation of an apparatus and process for producing and depositing molten silica particles to build up a large, fused silica boule. The apparatus, generally designated by the numeral 10, includes a feedstock source 12. Nitrogen, or a nitrogen/oxygen mixture, is used as the carrier gas.
A bypass stream of nitrogen 14 is introduced to prevent saturation ofthe vaporous stream. The vaporous reactant is passed through a distribution mechamsm to the reaction site wherein a number of burners 18 are present in close proximity to a furnace crown 20. The reactant is combined with a fuel oxygen mixture 22 at these burners, and is combusted and oxidized to deposit silica at a temperature greater than 1 00° C. High purity metal oxide soot and heat are directed downwardly through the refractory fumace crown 20. The silica is immediately deposited and consolidated to a non-porous mass 24 on hot cup 26.
Improvement in the zircon refractory, as disclosed in the Sempoiinski et al. patents, alleviated the affect of sodium ion contamination in a fused silica article However, it was then found that other contaminants also exist in the fumace refractory in addition to sodium These include the alkaline earth metals, and transition metals, such as iron, titanium and lead, aluminum, phosphorous and sulfur.
These metal contaminants have varying degrees of volatility at temperatures in excess of 1650°C, the temperature at which fused silica is deposited. Thus, they may be present in the fumace atmosphere, and become entrapped in the fused silica as it is deposited. The presence of these contaminating metals in a fused silica lens results in a reduction ofthe transmittance capability ofthe glass, and also results in development of an undesirable fluorescence in the glass. These deficiencies continue to further develop as the lens is subjected to short wavelength UV radiation in service. There are inherent variations in the metal impurity levels in a refractory material, as well as varying degrees of metal volatility. This makes it difficult to control glass quality in a fused silica collection fumace, or even to obtain acceptable glass frequently.
The problem becomes particularly acute when a polysiloxane is used as a precursor material for the fused silica. As explained in the Sempoiinski et al. patents, the self- cleansing action ofthe HCl by-product from a SiCl4 decomposition is lost with the siloxane precursor.
Contaminating metals can be present in the raw materials employed in production of fumace refractories. The metals may also be entrained during sintering ofthe refractory, or during any subsequent operations, such as sawing or grinding. Zircon is a relatively clean refractory, particularly when prepared as described in the Sempoiinski et al. patents. However, the superior transmission properties required for such demanding uses as microlithography applications require control of all metal contaminants at a level below 100 parts per billion (ppb).
We have found that this degree of contaminating metal control in a collection fumace can be achieved by constructing the furnace of refractory materials containing less than 300 parts per million (ppm) ofthe contaminating metals. In particular, we have found this to be true for zircon refractories used in a collection furnace for fused silica deposition. This desirable end is accomplished, in accordance with the present invention, by firing the fumace refractories in a halogen-containing atmosphere. The halogen reacts with and removes the contaminating metals from at least the exposed surface ofthe refractory.
We have found that chlorine or fluorine, alone or in acid gas form, to be especially useful. The cleansing gas can be used in essentially pure form. However, we have found it convenient, and effective, to employ as little as 5% ofthe cleansing gas in an inert gas, such as helium or argon, with a somewhat longer treatment time. The cleansing treatment may employ a continuous flow ofthe halogen gas. Alternatively, a pulsed type treatment may be used wherein gas is repeatedly introduced into the firing chamber and subsequently exhausted.
The cleansing action can occur at a temperature as low as 700°C. However, it is usually preferred to employ somewhat higher temperatures in the range of 1100 to 1500°C. Above 1500°C, zircon starts to thermally dissociate, thereby resulting in a weaker refractory body.
The invention is here described with reference to treatment of zircon refractory fumace elements. However, it will be appreciated that it is also applicable to cleansing contaminating metals from other types of refractory articles. The cleansing process on a refractory body may be carried out either prior to assembly into a fumace or after assembly. The treatment may also be carried out during production ofthe refractory. High temperature refractories, such as zircon, are sintered in air at temperatures in excess of 1500°C. As the sintered furnace components are being cooled, the cooling step can be interrupted at an appropriate temperature, for example, 1200°C. The sintering fumace is then switched to a halogen-containing atmosphere, and the temperature maintained for the necessary time to cleanse the refractory ofthe contaminating metals.
The use of refractories chemically cleaned in accordance with the invention provides several advantages. The cleaner deposition fumace provides a fused silica product of high purity. It provides high, consistent yields of fused silica glass having an acceptably high transmission of short wavelength UV radiation and a low level of fluorescence. Further, the glass is less prone to increases in radiation damage and fluorescence in service. These desired ends are achieved without requiring change in, or compromise of, either the fumace design or the silica forming and deposition process.
This is highly significant because these features are critical to achievement of refractive index homogeneity in the glass.
The effectiveness ofthe cleansing treatment was demonstrated by comparing two sets of fused silica test pieces. One set was taken from boules deposited in an untreated collection fumace. A second set was taken from boules deposited in a treated fumace.
The fiirnaces were constructed in essentially identical design with sintered zircon refractory crowns and cup liners. The refractories in the treated fumace were soaked for eight hours in a furnace operating at 1300°C. A flowing atmosphere of 5.7% Cl2 and
94.3% helium was maintained during the entire time.
Relevant properties were measured on the test pieces taken from comparable locations in the boules from the untreated fumace and those from the treated fumace. TABLE I shows internal transmittance in percent as determined on the basis of measurements for both 248 nm and 193 nm wavelength radiation.
TABLE I
Untreated Iieal≤-i 248 nm 99.08 99.82
99.46 99.85
193 nm 95.28 99.18
The fused silica boules described above were also analyzed to determine the percentage of boule depth that exhibited an acceptable low level of fluorescence.
Fluorescence is determined by integrating the intensities measured over the range of 400- 700 nm. To be acceptable, a glass test piece must exhibit a value, as so determined, that is below 4.2x10'9 watts/cm2 when the glass is exposed to an emitting laser operating at 15 mj/cm2 and 200 Hz. Glass from the untreated fumace was completely unacceptable. There was no portion ofthe boule in which the fluorescence value was acceptably low. Glass from the treated fumace had acceptable glass to a depth of 3.53 inches. This represented 59.3% of the total depth.

Claims

WE CLAIM:
1. An improved method of producing a fused silica body by introducing a silicon- containing compound into a flame to form molten silica particles and collecting those particles in the form of a fused silica body in a furnace constructed of refractory materials, the improvement comprising collecting the silica particles in a fumace at least a portion of which has been exposed to a reactive, halogen-containing gas to react with, and thereby cleanse the refractory of, contaminating metals.
2. A method in accordance with claim 1 in which refractory fumace components are exposed to the reactive, halogen-containing gas prior to being assembled in the fumace.
3. A method in accordance with claim 2 in which refractory fumace components are exposed to the reactive, halogen-containing gas as the refractory is being cooled during a sintering cycle.
4. A method in accordance with claim 1 in which the refractory components are exposed to the halogen-containing gas after the fumace is assembled.
5. A method in accordance with claim 1 in which the refractory components are exposed to a continuous flow of gas containing the halogen-containing gas.
6. A method in accordance with claim 1 in which the refractory components are exposed to a pulsed treatment with the halogen-containing gas.
7. A method in accordance with claim 1 in which the refractory components are exposed to an otherwise inert atmosphere containing 5-100% ofthe halogen-containing gas.
8. A method in accordance with claim 1 in which the refractory components are exposed to a halogen-containing gas at a temperature of 70O°-15O0°C.
9. A method in accordance with claim 8 in which the temperature of treatment is in the range of 1100°-1500°C.
10. A method in accordance with claim 1 in which the concentration of contaminating metal ions in the refractory components is reduced to less than 300 ppm.
11. A relatively pure fused silica article having a content of contaminating metal ions less than 100 ppb.
12. A fused silica lens in accordance with claim 11 in which the lens has a transmittance of at least 99.5% for radiation of 248 nm wavelength and a transmittance value of at least 98% for radiation of 193 nm wavelength.
13. A fused silica article in accordance with claim 11 in which at least about half the depth ofthe article is useful glass for laser lenses.
14. A refractory fumace for collecting molten silica particles in the form of a solid body, at least a portion ofthe furnace refractory having a content of metal contaminants less than 300 ppm.
15. A refractory fumace in accordance with claim 14 in which at least the inner surface ofthe refractory has been treated with a halogen-containing gas to react with contaminating metal ions.
16. A refractory fumace in accordance with claim 14 in which the refractory is zircon.
PCT/US1997/001681 1996-02-15 1997-02-11 Pure fused silica, furnace and method WO1997030933A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP97905726A EP0881987A4 (en) 1996-02-21 1997-02-11 Pure fused silica, furnace and method
US09/117,980 US6096761A (en) 1996-02-15 1997-02-11 Esters of 3-hydroxy-piperidinemethanol derivatives
US09/125,208 US6174509B1 (en) 1997-02-11 1997-02-11 Pure fused silica, furnace and method
JP9530179A JP2000505036A (en) 1996-02-21 1997-02-11 Pure fused silica, furnace and method

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US1199796P 1996-02-21 1996-02-21
US60/011,997 1996-02-21

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1030822A1 (en) * 1997-09-24 2000-08-30 Corning Incorporated FUSED SiO 2?-TiO 2? GLASS METHOD
EP1160209A2 (en) * 2000-05-30 2001-12-05 Tosoh Quartz Corporation Method and apparatus for manufacturing quartz glass ingot
US6410192B1 (en) 1999-11-15 2002-06-25 Corning Incorporated Photolithography method, photolithography mask blanks, and method of making
EP1358132A1 (en) * 2000-12-21 2003-11-05 Corning Incorporated Refractories for fused silica production furnaces
US9399585B2 (en) 2010-12-02 2016-07-26 Saint-Gobain Ceramics & Plastics, Inc. Zircon components
CN107873049A (en) * 2015-06-10 2018-04-03 康宁股份有限公司 The method that metal deposit is removed from glass

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2239551A (en) * 1939-04-22 1941-04-22 Corning Glass Works Method of making sealing glasses and seals for quartz lamps
US2272342A (en) * 1934-08-27 1942-02-10 Corning Glass Works Method of making a transparent article of silica
JPS54134721A (en) * 1978-04-11 1979-10-19 Nippon Telegraph & Telephone Manufacture of anhydrous glass parent material for optical fiber
JPS54160414A (en) * 1978-06-08 1979-12-19 Nippon Telegraph & Telephone Production of optical communication fiber material
US4552576A (en) * 1983-08-22 1985-11-12 The Furukawa Electric Co., Ltd. Method of fabricating optical glass base material and apparatus for fabricating the same
US4956059A (en) * 1988-10-29 1990-09-11 Heraeus Quarzschmelze Gmbh Process for the purification of granular silicon dioxide
US5043002A (en) * 1990-08-16 1991-08-27 Corning Incorporated Method of making fused silica by decomposing siloxanes
US5332702A (en) * 1993-04-16 1994-07-26 Corning Incorporated Low sodium zircon refractory and fused silica process

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA936790A (en) * 1971-03-31 1973-11-13 J. Kriegler Rudolph Sio2 structure having resistance to mobile ion contaminates and method for obtaining same

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2272342A (en) * 1934-08-27 1942-02-10 Corning Glass Works Method of making a transparent article of silica
US2239551A (en) * 1939-04-22 1941-04-22 Corning Glass Works Method of making sealing glasses and seals for quartz lamps
JPS54134721A (en) * 1978-04-11 1979-10-19 Nippon Telegraph & Telephone Manufacture of anhydrous glass parent material for optical fiber
JPS54160414A (en) * 1978-06-08 1979-12-19 Nippon Telegraph & Telephone Production of optical communication fiber material
US4552576A (en) * 1983-08-22 1985-11-12 The Furukawa Electric Co., Ltd. Method of fabricating optical glass base material and apparatus for fabricating the same
US4956059A (en) * 1988-10-29 1990-09-11 Heraeus Quarzschmelze Gmbh Process for the purification of granular silicon dioxide
US5043002A (en) * 1990-08-16 1991-08-27 Corning Incorporated Method of making fused silica by decomposing siloxanes
US5332702A (en) * 1993-04-16 1994-07-26 Corning Incorporated Low sodium zircon refractory and fused silica process
US5395413A (en) * 1993-04-16 1995-03-07 Corning Incorporated Method for producing fused silica with low sodium ion contamination level

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP0881987A4 *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1030822A1 (en) * 1997-09-24 2000-08-30 Corning Incorporated FUSED SiO 2?-TiO 2? GLASS METHOD
EP1030822A4 (en) * 1997-09-24 2004-12-15 Corning Inc FUSED SiO2-TiO2 GLASS METHOD
US6410192B1 (en) 1999-11-15 2002-06-25 Corning Incorporated Photolithography method, photolithography mask blanks, and method of making
US6475682B2 (en) 1999-11-15 2002-11-05 Corning Incorporated Photolithography method, photolithography mask blanks, and method of making
EP1160209A2 (en) * 2000-05-30 2001-12-05 Tosoh Quartz Corporation Method and apparatus for manufacturing quartz glass ingot
EP1160209A3 (en) * 2000-05-30 2002-07-03 Tosoh Quartz Corporation Method and apparatus for manufacturing quartz glass ingot
EP1358132A1 (en) * 2000-12-21 2003-11-05 Corning Incorporated Refractories for fused silica production furnaces
EP1358132A4 (en) * 2000-12-21 2004-12-29 Corning Inc Refractories for fused silica production furnaces
US6923021B2 (en) 2000-12-21 2005-08-02 Corning Incorporated Method and apparatus for fused silica production
US9399585B2 (en) 2010-12-02 2016-07-26 Saint-Gobain Ceramics & Plastics, Inc. Zircon components
US9403689B2 (en) 2010-12-02 2016-08-02 Saint-Gobain Ceramics & Plastics, Inc. Zircon components
CN107873049A (en) * 2015-06-10 2018-04-03 康宁股份有限公司 The method that metal deposit is removed from glass

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EP0881987A4 (en) 1999-05-12
EP0881987A1 (en) 1998-12-09

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