[특허]Process for melting and refining silica-based glass

Owens Brocking Glass Container Inc.

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Process for melting and refining silica-based glass

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	C03B-005/173 C03B-005/225
미국특허분류(USC)	065/134.9; 065/134.2
출원번호	US-0288681 (2011-11-03)
등록번호	US-8910497 (2014-12-16)
발명자 / 주소	Leidy, D. Wayne Dewet-Smith, Dawid Fayerweather, Carl L. Hixson, Brett E.
출원인 / 주소	Owens Brocking Glass Container Inc.
인용정보	피인용 횟수 : 1 인용 특허 : 9

초록
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A process for making silica-based glass includes: (a) forming a glass precursor melt that includes glass network formers and glass network modifiers, the glass precursor melt being at a temperature in the range of 900 C to 1700 C and having a viscosity of not more than 3 Pa·s, and (b) refining the glass precursor melt. Either or both steps (a) and (b) can include stirring and/or be carried out under reduced pressure to enhance refining. The refined glass precursor melt preferably is mixed with additional materials including silica (SiO2) to form a silica...

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1. A process for making a glass product melt composition, which includes the steps of: (a) providing a first mixture of raw materials that includes a glass network former and gas releasing glass network modifiers;(b) providing a second mixture of raw materials that includes an additional amount of said glass network former and non-gas releasing glass network modifiers;(c) melting and reacting said first mixture of raw materials to form a glass precursor melt having a temperature in the range of 900 C to 1700 C and having a viscosity of not more than 3 Pa·s;(d) refining said glass precursor melt, wherein said viscosity of said glass precursor melt promotes release of gaseous reactions products from said precursor melt that evolved upon decomposition of said gas releasing glass network modifiers in said step (c); and then(e) dissolving said second mixture of raw materials in said refined glass precursor melt to form a final glass melt that has a greater percentage of said glass network former than said glass precursor melt. 2. The process set forth in claim 1 wherein said step (d) includes performing said step (c) under reduced pressure. 3. The process set forth in claim 1 wherein said glass network former is selected from the group consisting of compounds of Si, Al and B. 4. The process set forth in claim 3 wherein said glass network former is selected from the group consisting of the oxide, sulfide or acid forms of the recited elements. 5. The process set forth in claim 1 wherein substantially all gas releasing glass network modifiers required to form said final glass melt in said step (e) are provided in said step (a). 6. The process set forth in claim 1 wherein said glass network modifiers are selected from the group consisting of elements and compounds of sodium (Na), lithium (Li), potassium (K), calcium (Ca), magnesium (Mg), and barium (Ba). 7. The process set forth in claim 6 wherein said gas releasing glass network modifiers are selected from the group consisting of the carbonate, bicarbonate, sulfate, hydrate, hydroxide, nitrate, chloride or acid forms of the recited elements. 8. The process set forth in claim 6 wherein said non-gas releasing glass network modifiers are selected from the group consisting of the oxide, sulfide or elemental forms of the recited elements. 9. The process set forth in claim 1 wherein said glass precursor melt includes at least one alkali metal and at least one alkaline earth metal and has an alkali metal to alkaline earth metal molar ratio of 1:3 to 3:1. 10. The process set forth in claim 1 wherein said glass precursor melt has a molar ratio of glass network modifiers to glass network formers of 2:1.5 to 1:2. 11. The process set forth in claim 1 wherein said step (e) is carried out at a temperature greater than about 900 C. 12. The process set forth in claim 1 wherein said step (e) includes stirring. 13. The process set forth in claim 1 wherein said second mixture of raw materials includes cullet. 14. The process set forth in claim 1 wherein said glass network modifiers are selected from the group consisting of compounds of alkali metals and compounds of alkaline earth metals. 15. The process set forth in claim 1 wherein said glass network former is silica (SiO2) and said glass melt formed in said step (e) includes 65-80 wt. % silica (SiO2). 16. A process for making a glass product melt composition, which includes the steps of: (a) forming a glass precursor melt by melting and reacting a mixture of raw materials that includes a glass network former and one or more as releasing glass network modifiers, wherein said glass network modifiers and said glass network former are mixed together at a molar ratio in the range of 2:1.5 to 1:2 such that said glass precursor melt has a desired low viscosity at a temperature in the range of 900 C to 1700 C;(b) refining said glass precursor melt, wherein said low viscosity of said glass precursor melt promotes release of gaseous reactions products from said glass precursor melt that evolved upon decomposition of said one or more as releasing glass network modifiers in said step (a); and then(c) dissolving additional raw materials in said refined glass precursor melt to form a glass product melt composition having a higher viscosity than said glass precursor melt at the same temperature. 17. The process set forth in claim 16 wherein said glass precursor melt has a viscosity of not more than 3 Pa·s during said step (b). 18. The process set forth in claim 16 including: stirring said glass precursor melt during said step (c) to promote dissolution of said additional raw materials and homogenization of said glass product melt composition. 19. The process set forth in claim 16 wherein said one or more gas releasing glass network modifiers include substantially all gas releasing glass network modifiers that are required to achieve said glass product melt composition. 20. The process set forth in claim 16 wherein said glass product melt composition has a greater percentage of said glass network former than said glass precursor melt. 21. The process set forth in claim 16 wherein said step (c) includes dissolving an additional amount of said glass network former in said glass precursor melt to achieve said glass product melt composition. 22. The process set forth in claim 16 wherein the amount of said glass network former in said glass precursor melt is less than the total amount of said glass network former that is required to achieve said glass product melt composition. 23. The process set forth in claim 16 wherein said steps (a) and (b) are performed in not more than 2 hours. 24. The process set forth in claim 16 wherein said step (b) is performed under reduced pressure to promote release of gaseous reaction products from said glass precursor melt. 25. The process set forth in claim 16 wherein said step (b) is carried out at a temperature in the range of 1250 C to 1450 C. 26. The process set forth in claim 16 wherein said step (c) includes dissolving non-gas releasing glass network modifiers in said glass precursor melt to achieve said glass product melt composition. 27. A process for making a glass product melt composition, which includes the steps of: (a) providing raw materials including a glass network former and gas releasing glass network modifiers, wherein said glass network former is selected from the group consisting of elements and compounds of silicon (Si), aluminum (Al), and boron (B) and said gas releasing glass network modifiers are selected from the group consisting of compounds of alkali metals and compounds of alkaline earth metals;(b) melting and reacting said raw materials to form a precursor solution in liquid phase having a glass network modifier to glass network former molar ratio in the range of 2:1.5 to 1:2 such that said precursor solution has a desired low viscosity at a temperature in the range of 900 C to 1700 C;(c) refining said precursor solution, wherein said low viscosity of said precursor solution promotes release of gaseous reactions products from said precursor solution that evolved upon decomposition of said gas releasing glass network modifiers in said step (b); and then(d) dissolving additional raw materials in said precursor solution to form a final glass melt, wherein said additional raw materials include an additional amount of said glass network former and said final glass melt includes a greater percentage of said glass network former than said precursor solution. 28. The process set forth in claim 27 wherein said glass network modifier to glass network former molar ratio provides said precursor solution with a viscosity of not more than 3 Pa·s. 29. The process set forth in claim 27 wherein the amount of said glass network former provided in said step (a) is less than the total amount of said glass network former that is required to achieve said glass product melt composition. 30. The process set forth in claim 27 wherein said glass network former provided in said step (a) is silica (SiO2). 31. The process set forth in claim 30 wherein said precursor solution includes 40-60 mol. % silica (SiO2). 32. The process set forth in claim 30 wherein said final glass melt formed in said step (d) includes 65-80 wt. % silica (SiO2). 33. The process set forth in claim 30 wherein said precursor solution formed in said step (b) is a sodium-calcium-silicate precursor solution that has a sodium:calcium:silicon molar ratio in the range of 1:1:1.5 to 1:1:4. 34. The process set forth in claim 27 wherein said additional raw materials dissolved in said precursor solution in said step (d) include a non-gas releasing glass network modifier selected from the group consisting of elements, sulfides, and oxides of alkali metals and elements, sulfides, and oxides of alkaline earth metals.

이 특허에 인용된 특허 (9)

이 특허를 인용한 특허 피인용횟수: 1

Dewet-Smith, Dawid; Leidy, D. Wayne; Fayerweather, Carl L.; Swiler, Daniel R.; Clark, Terence J.. Apparatus for melting and refining silica-based glass. USP2017059637406.

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Process for melting and refining silica-based glass

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