Refining Glass with Reduced Pressure
US-2019284078-A1 · Sep 19, 2019 · US
US11339077B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11339077-B2 |
| Application number | US-201916668115-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 30, 2019 |
| Priority date | Oct 30, 2019 |
| Publication date | May 24, 2022 |
| Grant date | May 24, 2022 |
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Official abstract text for this publication.
A glass fining system, glass fining device, and method are disclosed. The glass fining device in accordance with one aspect of the disclosure includes at least one heated orifice through which molten glass flows from a glass melter to produce at least one superheated glass stream; and a low-pressure chamber disposed downstream from the heated orifice, where the at least one superheated glass stream flows from the at least one heated orifice and into the low-pressure chamber, and where the low-pressure chamber surrounds the at least one superheated glass stream. In some embodiments, the low-pressure chamber may include at least one surface extender.
Opening claim text (preview).
The invention claimed is: 1. A glass fining device, comprising: at least one heated orifice device including at least one orifice through which molten glass flows directly from a glass melter through the at least one heated orifice device, said at least one heated orifice device capable of heating said molten glass to a superheated temperature above that of a temperature of the molten glass to produce at least one superheated glass stream; a low-pressure chamber disposed downstream from and connected directly to the at least one heated orifice device, where the at least one superheated glass stream flows directly from the at least one heated orifice device and into the low-pressure chamber, and where the low-pressure chamber surrounds the at least one superheated glass stream and is at a pressure less than atmospheric pressure, said low-pressure chamber insulated to maintain said at least one superheated glass stream at said superheated temperature; and said low-pressure chamber providing a residence time of said at least one superheated glass stream in said low-pressure chamber of from 1 minute to 10 minutes. 2. The glass fining device in claim 1 , wherein the at least one heated orifice device includes a plurality of orifices. 3. The glass fining device in claim 1 , wherein the at least one heated orifice device includes an electrode orifice. 4. The glass fining device in claim 1 , wherein the at least one heated orifice device heats the molten glass to a superheated temperature of between 1400° C. and 1700° C. 5. The glass fining device in claim 1 , wherein the at least one heated orifice device and the low-pressure chamber are aligned with a vertically inline fining axis. 6. The glass fining device in claim 1 , wherein the low-pressure chamber is at a pressure of from 20-600 torr. 7. The glass fining device in claim 1 , wherein the low-pressure chamber includes at least one surface extender. 8. The glass fining device in claim 7 , wherein the at least one surface extender is an induction heat surface extender. 9. The glass fining device in claim 7 , wherein the at least one surface extender is a water cooled surface extender. 10. The glass fining device in claim 7 , wherein the at least one surface extender includes at least one of a pole, a sphere, or a sloped wall. 11. A glass fining system, comprising: a glass melter; and a glass fining device directly coupled to the glass melter, including at least one heated orifice device through which molten glass from said glass melter flows, said at least one heated orifice device producing at least one superheated glass stream flows from the glass melter, said superheated glass stream having a superheated temperature above a temperature of the molten glass; a low-pressure chamber disposed downstream from and directly connected to the at least one heated orifice device, where the at least one superheated glass stream flows directly from the at least one heated orifice device and into the low-pressure chamber, and where the low-pressure chamber surrounds the at least one superheated glass stream and is at a pressure less than atmospheric pressure, said low-pressure chamber insulated to maintain said at least one superheated glass stream at said superheated temperature; and said low-pressure chamber providing a residence time of said at least one superheated glass stream of from 1 minute to 10 minutes. 12. The glass fining system in claim 11 , wherein the glass melter includes a submerged combustion melter. 13. A method for fining molten glass, comprising: melting glass in a glass melter; flowing the molten glass having a molten glass temperature from the glass melter directly through at least one heated orifice device, the at least one heated orifice device heating the molten glass resulting in a superheated glass stream having a superheated temperature above the molten glass temperature; and flowing the at least one superheated glass stream from the at least one heated orifice device directly into a low-pressure chamber, wherein the low-pressure chamber surrounds the at least one superheated glass stream, is at a pressure less than atmospheric pressure, is insulated to maintain the superheated glass stream at the superheat temperature and provides a residence time for the superheated glass stream of from 1 minute to 10 minutes. 14. The method for fining molten glass in claim 13 , wherein the glass melter is a submerged combustion melter. 15. The method for fining molten glass in claim 13 , wherein the at least one heated orifice device is an electrode orifice. 16. The method for fining molten glass in claim 13 , wherein the at least one heated orifice device heats the molten glass to a superheated temperature of between 1400° C. and 1700° C. 17. The glass fining device in claim 13 , wherein the low-pressure chamber is at a pressure of from 20-600 torr. 18. The method for fining molten glass in claim 13 , wherein flowing the superheated glass stream includes flowing the superheated glass stream parallel to a vertically inline fining axis. 19. The method for fining molten glass in claim 13 , further comprising: flowing the at least one superheated glass stream over at least one surface extender. 20. The method for fining molten glass in claim 19 , wherein the at least one surface extender includes an induction heat surface extender. 21. The method for fining molten glass in claim 19 , wherein the at least one surface extender includes a water cooled surface extender. 22. The method for fining molten glass in claim 19 , wherein the at least one surface extender includes at least one of a pole, a sphere, or a sloped wall.
Outlets {, e.g. drains, siphons}; Overflows {, e.g. for supplying the float tank, tweels} · CPC title
in electric furnaces {, e.g. by dielectric heating (electric heating in general H05B)} · CPC title
by thin-layer fining · CPC title
Submerged heating, e.g. by using heat pipes, hot gas or submerged combustion burners (bubblers C03B5/193) · CPC title
under reduced pressure, e.g. with vacuum refiners · CPC title
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