US20040107732A1 - Apparatus and method for producing float glass having reduced defect density - Google Patents
Apparatus and method for producing float glass having reduced defect density Download PDFInfo
- Publication number
- US20040107732A1 US20040107732A1 US10/672,026 US67202603A US2004107732A1 US 20040107732 A1 US20040107732 A1 US 20040107732A1 US 67202603 A US67202603 A US 67202603A US 2004107732 A1 US2004107732 A1 US 2004107732A1
- Authority
- US
- United States
- Prior art keywords
- glass
- section
- float
- float chamber
- threshold temperature
- 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.)
- Abandoned
Links
- 239000005329 float glass Substances 0.000 title claims abstract description 18
- 230000007547 defect Effects 0.000 title claims description 24
- 238000004519 manufacturing process Methods 0.000 title description 4
- 239000011521 glass Substances 0.000 claims abstract description 55
- 239000001257 hydrogen Substances 0.000 claims abstract description 25
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 25
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 19
- 239000000446 fuel Substances 0.000 claims description 24
- 239000007789 gas Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000000156 glass melt Substances 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 229910052681 coesite Inorganic materials 0.000 claims description 2
- 229910052593 corundum Inorganic materials 0.000 claims description 2
- 229910052906 cristobalite Inorganic materials 0.000 claims description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 229910052682 stishovite Inorganic materials 0.000 claims description 2
- 229910052905 tridymite Inorganic materials 0.000 claims description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 238000000576 coating method Methods 0.000 description 11
- 239000006060 molten glass Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 10
- 238000006124 Pilkington process Methods 0.000 description 9
- 239000011248 coating agent Substances 0.000 description 9
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 239000006066 glass batch Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000008246 gaseous mixture Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000002238 attenuated effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000004320 controlled atmosphere Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000005361 soda-lime glass Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B18/00—Shaping glass in contact with the surface of a liquid
- C03B18/02—Forming sheets
- C03B18/20—Composition of the atmosphere above the float bath; Treating or purifying the atmosphere above the float bath
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B18/00—Shaping glass in contact with the surface of a liquid
- C03B18/02—Forming sheets
- C03B18/18—Controlling or regulating the temperature of the float bath; Composition or purification of the float bath
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
- C03B5/2353—Heating the glass by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances
-
- 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
- C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
- C03C3/083—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound
- C03C3/085—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal
- C03C3/087—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal containing calcium oxide, e.g. common sheet or container glass
-
- 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
-
- 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
Definitions
- the present invention relates to a float glass chamber used to produce flat glass by the float glass process, and more specifically float glass chambers that can be used to yield glass having reduced defect density.
- the float glass process is well known for making sheets of glass.
- batch materials are heated to form molten glass.
- the molten glass is then poured onto a bath of molten tin.
- the molten glass is drawn along the bath of molten tin and simultaneously cooled and attenuated to form a dimensionally stable continuous sheet of glass, typically referred to as a glass ribbon.
- the sheet is then removed from the bath for further processing.
- an oxy-fuel furnace In an oxy-fuel furnace, oxygen, not air, supports combustion. As a result, an oxy-fuel furnace provides a much more efficient melt than an air-fuel furnace because energy is no longer being wasted heated up nitrogen in the air and oxy-fuel flames have a higher flame temperature which radiates more efficiently. The increased melting efficiency allows more tonnage to be processed through an oxy-fuel furnace than through a similarly sized, air-fuel furnace.
- Both air-fuel and oxy-fuel furnaces have water in their atmospheres.
- the head space (the area of the furnace above the molten glass) in an oxy-fuel furnace has a higher concentration of water than in an air-fuel furnace because the oxy-fuel atmosphere lacks the nitrogen provided in an air-fired furnace that dilutes the total water formed by combustion.
- the water typically constitutes about 66% by volume of the head space in an oxy-fuel furnace versus 18% in an air-fired furnace. Since the amount of water in the glass melt is proportional to the square root of the concentration of water in the head space, glass melted in an oxy-fuel furnace has a 1.7 to 2 times higher water concentration than glass melted in a conventional air-fuel furnace. Typically, glass melted in an oxy-fuel furnace contains more than 0.045 weight percent water based on the total weight of the composition.
- the molten tin temperature in the float bath ranges from 1800° F. to 1900° F. (981° C. to 1037° C.).
- 1800° F. at the glass-tin interface, water that diffuses out of the molten glass dissociates into hydrogen and oxygen. Because hydrogen isn't very soluble in tin at 1800° F., much of the hydrogen does not dissolve in the tin but remains in the atmosphere of the bath.
- open bottom bubbles Some of the hydrogen from the disassociation of water gets trapped at the interface between the molten glass and tin and ultimately impinges on the bottom surface of the glass ribbon and form defects along the ribbon surface typically referred to as open bottom bubbles.
- the open-bottom bubbles can be described as voids in glass that generally have an inverted-U shape cross-section. The presence of open bottom bubbles increases the overall defect density of the glass.
- the present invention provides a novel apparatus and method that yields float glass having a lower total defect density as a result of reduced open bottom bubble defects.
- the present invention is float glass chamber comprising:
- a hot section having an atmosphere in at least the lower plenum comprises less than 3 percent hydrogen based on volume
- a cold section wherein the boundary line between the hot section and the cold section is where the temperature of the glass falls below a threshold temperature.
- the present invention is method for making float glass with reduced defect density comprising:
- the hot section has an atmosphere in at least the lower plenum comprises less than 3 percent hydrogen based on volume
- FIG. 1. is a sectional view of a float chamber according to the present invention, with portions removed for clarity.
- a stated range of “1 to 10” should be considered to include any and all subranges between (and inclusive of) the minimum value of 1 and the maximum value of 10; that is, all subranges beginning with a minimum value of 1 or more and ending with a maximum value of 10 or less, e.g., 5.5 to 10 or 3.2 to 7.8.
- a glass batch composition is heated to a molten state and poured into the float chamber.
- the float chamber has a refractory roof 3 that divides the chamber into an upper plenum 1 and a lower plenum 2 .
- the lower plenum contains the glass 4 and the tin 5 .
- the upper plenum contains all of the overhead electrical heating elements to provide controlled heating of the liquid metal float bath and the formed glass ribbon.
- a controlled atmosphere is maintained in the chamber via gas inlets 6 and gas outlet(s) 7 .
- the novel float glass chamber of the present invention comprises at least two sections—a hot section and a cold section.
- the boundary line between the hot section and the cold section is where the temperature of the glass falls below a predetermined temperature, hereinafter referred to as the “threshold temperature,” required for glass in the hot section.
- the threshold temperature a predetermined temperature
- the threshold temperature is 2100° F. In another non-limiting embodiment of the invention, the threshold temperature is 1800° F. In another non-limiting embodiment of the invention, the threshold temperature is 1600° F. The lower the threshold temperature for the hot section, the larger the hot section and the smaller the cold section and visa versa.
- the hot section of the chamber is approximately 90 to 100 feet from the point where the molten glass is poured onto the tin.
- the cold section of the chamber is the next approximately 70 to 140 feet of chamber behind the hot section, depending on the size of the bath.
- numerous gas inlets and outlets are present in the upper plenum and lower plenum of the float chamber.
- Various gaseous mixtures can be pumped into the chamber through the gas inlets or out of the chamber through the gas outlets to control the atmosphere within the chamber.
- the gas inlets to at least the lower plenum over the hot section of the chamber deliver in a gas comprising less than 1 weight percent hydrogen based on volume.
- the remainder of the gas can be an inert gas, such as but not limited to nitrogen.
- the atmosphere of the lower plenum over the hot section of the chamber can comprise 3 percent hydrogen based on volume.
- the atmosphere of the lower plenum over the hot section of the chamber can comprise 1 percent hydrogen based on volume.
- Various mixtures of hydrogen and nitrogen or argon or ammonia in placed of mixed gases can be pumped into the atmosphere of at least the lower plenum over the cold section of the chamber.
- the gaseous mixture can comprise up to 10 percent of the hydrogen based on volume.
- the rest of the gas can be nitrogen.
- the gas outlets in the float chamber can be used to remove gas from the chamber.
- up to 40 volume percent based on volume of the total flow of the gas pumped into the chamber as discussed above can be removed from the hot section.
- the present invention also encompasses a method for producing glass.
- glass can be produced via the following steps: adding glass batch materials to a furnace; melting the batch materials; pouring molten glass from the furnace into the float chamber; and removing the float glass from the float chamber.
- the first step of the present invention comprises adding glass batch materials to a furnace.
- the furnace can be an air-fuel furnace or an oxy-fuel furnace.
- the glass batch materials can be of any conventional type including, but not limited to, conventional soda-lime-silica glass batch materials.
- a conventional glass composition can be characterized as follows:
- the third step of the present invention involves pouring molten glass from the furnace into the float chamber.
- the molten glass flows onto the top of the molten tin and moves along the top of the tin from the hot section of the chamber to the cold section of the chamber.
- the temperature of the glass in the hot section and the cold section of the chamber are as discussed above.
- the environments above the glass in the hot section and the cold section of the chamber are as discussed above.
- the glass melt coming into the tin bath can contain water.
- the glass melt can have a water content equal to or greater than 0.045 weight percent based on the total weight percent of the composition.
- the next step of the invention involves removing the float glass from the bath as is well known in the art.
- the glass can also be coated.
- the glass is coated.
- the coating can include one or more coating layers and/or coating films.
- the coating can be of any desired type.
- the coating can be an electroconductive coating, a heatable coating, an antenna coating, or a solar control coating, such as a low emissivity coating.
- Non-limiting examples of solar control and antenna coatings are disclosed in U.S. Pat. Nos.
- Glass made by a float process typically ranges from a sheet thickness of 2 millimeter to 20 millimeters. Glass having the aforementioned thickness can be prepared on a conventional float line having a line speed ranging from 100 to 800 inches per minute. The required thickness of the glass is determined by the end use of the glass.
- Glass produced according to the present invention can meet the various commercial standards for defect density.
- car manufactures set standards for defect density for automotive windshields.
- One automobile manufacture requires-automotive windshield glass production to have less than 1 total defect per 100 square feet.
- the glass produced according to the present invention can be used as automotive transparencies, in colored glasses, laminated products, etc. as is well known in the art.
- a laminated product can comprise at least one piece of glass produced according to the present invention.
- Such a laminated product can be a windshield.
- the apparatus and method of the present invention allows float glass to be produced which has substantially reduced open-bottom bubble defects as compared to conventional float glass.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Glass Compositions (AREA)
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP03759549A EP1542935A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
| PCT/US2003/030576 WO2004028987A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
| CA2499949A CA2499949C (en) | 2002-09-27 | 2003-09-26 | Method for producing float glass having reduced defect density |
| AU2003275273A AU2003275273A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
| JP2004540235A JP5032744B2 (ja) | 2002-09-27 | 2003-09-26 | 減少した欠損密度を有するフロートガラスを生成するための装置および方法 |
| US10/672,026 US20040107732A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
| CNB038229552A CN100339321C (zh) | 2002-09-27 | 2003-09-26 | 用于生产具有减少的缺陷密度的浮法玻璃的装置和方法 |
| MXPA05003111A MXPA05003111A (es) | 2002-09-27 | 2003-09-26 | Aparato y metodo para producir vidrio flotado con una densidad de defecto reducida. |
| US11/760,194 US10280105B2 (en) | 2002-09-27 | 2007-06-08 | Apparatus and methods for producing float glass having reduced defect density |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US41451602P | 2002-09-27 | 2002-09-27 | |
| US10/672,026 US20040107732A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/760,194 Continuation US10280105B2 (en) | 2002-09-27 | 2007-06-08 | Apparatus and methods for producing float glass having reduced defect density |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20040107732A1 true US20040107732A1 (en) | 2004-06-10 |
Family
ID=32045292
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/672,026 Abandoned US20040107732A1 (en) | 2002-09-27 | 2003-09-26 | Apparatus and method for producing float glass having reduced defect density |
| US11/760,194 Expired - Lifetime US10280105B2 (en) | 2002-09-27 | 2007-06-08 | Apparatus and methods for producing float glass having reduced defect density |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/760,194 Expired - Lifetime US10280105B2 (en) | 2002-09-27 | 2007-06-08 | Apparatus and methods for producing float glass having reduced defect density |
Country Status (8)
| Country | Link |
|---|---|
| US (2) | US20040107732A1 (enExample) |
| EP (1) | EP1542935A1 (enExample) |
| JP (1) | JP5032744B2 (enExample) |
| CN (1) | CN100339321C (enExample) |
| AU (1) | AU2003275273A1 (enExample) |
| CA (1) | CA2499949C (enExample) |
| MX (1) | MXPA05003111A (enExample) |
| WO (1) | WO2004028987A1 (enExample) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070022780A1 (en) * | 2005-07-28 | 2007-02-01 | House Keith L | Method of increasing the effectiveness of a fining agent in a glass melt |
| US20070175241A1 (en) * | 2005-07-28 | 2007-08-02 | Delamielleure Megan A | Method of reducing gaseous inclusions in a glass making process |
| DE102009000348A1 (de) | 2008-08-28 | 2010-03-04 | Schott Ag | Verfahren zur Herstellung von Flachglas |
| DE102008041661A1 (de) | 2008-08-28 | 2010-03-04 | Schott Ag | Verfahren zur Herstellung von Flachglas und Floatbadvorrichtung |
| US20100199721A1 (en) * | 2008-11-12 | 2010-08-12 | Keisha Chantelle Ann Antoine | Apparatus and method for reducing gaseous inclusions in a glass |
| US9512026B2 (en) | 2012-03-14 | 2016-12-06 | Asahi Glass Company, Limited | Float glass plate and method of manufacturing thereof |
| US20230219835A1 (en) * | 2020-06-08 | 2023-07-13 | Bengbu China Optoelectronic Technology Co., Ltd | High-generation tft-lcd glass substrate production line |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7475568B2 (en) * | 2005-04-27 | 2009-01-13 | Corning Incorporated | Method of fining glass |
| EP2690072B1 (en) * | 2011-03-23 | 2019-12-04 | AGC Inc. | Float glass and process for producing same |
| EP3617158A1 (en) * | 2018-08-28 | 2020-03-04 | Linde Aktiengesellschaft | Method for manufacturing float glass |
| EP3941881B1 (en) * | 2019-03-20 | 2025-08-27 | Air Products and Chemicals, Inc. | Method for tin bath monitoring and control |
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| US3356476A (en) * | 1965-02-08 | 1967-12-05 | Pittsburgh Plate Glass Co | Method of removing contaminates from the protective atmosphere of a glass sheet float bath |
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| US3615315A (en) * | 1962-04-19 | 1971-10-26 | Ppg Industries Inc | Method and apparatus having sealing means and gaseous takeoff for float glass |
| US3337319A (en) * | 1962-10-17 | 1967-08-22 | Pilkington Brothers Ltd | Method and apparatus for purifying the molten bath of a glass sheet forming operation |
| NL299371A (enExample) * | 1962-10-17 | |||
| DE1596419B1 (de) * | 1967-04-01 | 1970-10-15 | Floatglas Gmbh | Verfahren zur kontinuierlichen Herstellung eines Flachglasbandes auf einem Bad aus geschmolzenem Zinn |
| US3584475A (en) * | 1967-04-14 | 1971-06-15 | Ppg Industries Inc | Float glass tank with a particulate bottom covering |
| US3607203A (en) * | 1967-07-07 | 1971-09-21 | Nippon Sheet Glass Co Ltd | Float glass apparatus with longitudinal dams and metal flow control means |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070022780A1 (en) * | 2005-07-28 | 2007-02-01 | House Keith L | Method of increasing the effectiveness of a fining agent in a glass melt |
| US20070175241A1 (en) * | 2005-07-28 | 2007-08-02 | Delamielleure Megan A | Method of reducing gaseous inclusions in a glass making process |
| US7584632B2 (en) | 2005-07-28 | 2009-09-08 | Corning Incorporated | Method of increasing the effectiveness of a fining agent in a glass melt |
| US7854144B2 (en) | 2005-07-28 | 2010-12-21 | Corning Incorporated | Method of reducing gaseous inclusions in a glass making process |
| DE102009000348A1 (de) | 2008-08-28 | 2010-03-04 | Schott Ag | Verfahren zur Herstellung von Flachglas |
| DE102008041661A1 (de) | 2008-08-28 | 2010-03-04 | Schott Ag | Verfahren zur Herstellung von Flachglas und Floatbadvorrichtung |
| DE102009000348B4 (de) * | 2008-08-28 | 2011-09-01 | Schott Ag | Verfahren zur Herstellung von Flachglas |
| DE102008041661B4 (de) * | 2008-08-28 | 2011-12-08 | Schott Ag | Verfahren zur Herstellung von Flachglas und Floatbadvorrichtung |
| US20100199721A1 (en) * | 2008-11-12 | 2010-08-12 | Keisha Chantelle Ann Antoine | Apparatus and method for reducing gaseous inclusions in a glass |
| US9512026B2 (en) | 2012-03-14 | 2016-12-06 | Asahi Glass Company, Limited | Float glass plate and method of manufacturing thereof |
| US20230219835A1 (en) * | 2020-06-08 | 2023-07-13 | Bengbu China Optoelectronic Technology Co., Ltd | High-generation tft-lcd glass substrate production line |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2006513118A (ja) | 2006-04-20 |
| MXPA05003111A (es) | 2005-06-22 |
| CN1684914A (zh) | 2005-10-19 |
| AU2003275273A1 (en) | 2004-04-19 |
| WO2004028987A1 (en) | 2004-04-08 |
| US20070227190A1 (en) | 2007-10-04 |
| CA2499949C (en) | 2012-02-07 |
| EP1542935A1 (en) | 2005-06-22 |
| CN100339321C (zh) | 2007-09-26 |
| JP5032744B2 (ja) | 2012-09-26 |
| CA2499949A1 (en) | 2004-04-08 |
| US10280105B2 (en) | 2019-05-07 |
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| AS | Assignment |
Owner name: PPG INDUSTRIES OHIO, INC., OHIO Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SMITH, CHARLENE S.;PECORARO, GEORGE A.;REEL/FRAME:014930/0708;SIGNING DATES FROM 20040107 TO 20040113 |
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| STCB | Information on status: application discontinuation |
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