Submerged combustion melters having an extended treatment zone and methods of producing molten glass

• US 10,392,285 B2
• Filed: 11/22/2016
• Issued: 08/27/2019
• Est. Priority Date: 10/03/2012
• Status: Active Grant

• Current Assignee: Johns Manville Corporation (Berkshire Hathaway Incorporated)
• Original Assignee: Johns Manville Corporation (Berkshire Hathaway Incorporated)
• Inventors: Charbonneau, Mark William, McHugh, Kevin Patrick, Huber, Aaron Morgan
• Primary Examiner(s): Snelting, Erin
• Application Number:
  US15/358,286
• Publication Number:
  US 20170073262A1
• Time in Patent Office: 1,008 Days
• Field of Search: 65347, 651341, 651345
• CPC Class Codes: C03B 2211/22 by direct combustion in the melt
• CPC Class Codes: C03B 2211/23 using oxygen, i.e. pure oxygen or oxygen-enriched air
• CPC Class Codes: C03B 2211/24 by direct contact of non-combusting hot gas in the melt
• CPC Class Codes: C03B 5/04 in tank furnaces C03B5/02 takes precedence
• CPC Class Codes: C03B 5/173 Apparatus for changing the composition of the molten glass in glass furnaces, e.g. for colouring the molten glass chemical aspects C03C
• CPC Class Codes: C03B 5/193 using gas, e.g. bubblers
• CPC Class Codes: C03B 5/20 Bridges, shoes, throats, or other devices for withholding dirt, foam, or batch
• CPC Class Codes: C03B 5/205 Mechanical means for skimming or scraping the melt surface
• CPC Class Codes: C03B 5/225 Refining C03B5/18 takes precedence ; Refining agents C03C1/004
• CPC Class Codes: C03B 5/2356 Submerged heating, e.g. by using heat pipes, hot gas or submerged combustion burners bubblers C03B5/193
• CPC Class Codes: Y02P 40/50 Glass production, e.g. reusing waste heat during processing or shaping

Abstract

A submerged combustion melter includes a floor, a roof, and a sidewall structure connecting the floor and roof defining an internal space. A first portion of the internal space defines a melting zone, and a second portion defines a fining zone immediately downstream of the melting zone. One or more combustion burners in either the floor, roof, the sidewall structure, or any combination of these, are configured to emit the combustion gases from a position under a level of, and positioned to transfer heat to and produce, a turbulent molten mass of glass containing bubbles in the melting zone. The fining zone is devoid of combustion burners or other apparatus or components that would increase turbulence above that in the melting zone. The melter may include a treating zone that stabilizes or destabilizes bubbles and/or foam. Processes of using the melters are a feature of the disclosure.

Claims

1. A submerged combustion melter comprising:

a floor, a roof, and a sidewall structure connecting the floor and roof defining an internal space, a first portion of the internal space comprising a melting zone, a second portion of the internal space defining a fining zone downstream of the melting zone, and a third portion of the internal space comprising a treating zone downstream of the melting zone and upstream of the fining zone, the treating zone comprising one or more apparatus configured to inject a treating composition into a molten mass of glass containing bubbles in the treating zone, the treating zone and the fining zone devoid of submerged combustion burners and other apparatus that would increase turbulence above that in the melting zone;

one or more combustion burners in either the floor, the roof, the sidewall structure, or any two or more of these, producing combustion gases and configured to emit the combustion gases from a position under a level of, and positioned to transfer heat to and produce, a turbulent molten mass of glass containing bubbles in the melting zone;

a skimmer having distal end adapted to extend to a point just above a level of molten mass of glass exiting the fining zone to hold back a portion of foam floating on the molten mass of glass flowing out of the fining zone;

the submerged combustion melter comprising a geometry whereby the level of the molten glass is substantially equivalent in the melting zone, the treatment zone, and the fining zone, wherein the floor in the melting zone is substantially horizontal and the floor in the fining zone is angled upward at an angle α

with respect to the substantially horizontal floor in the melting zone so that the floor in the fining zone is angled upward relative to horizontal beginning at an entrance to the fining zone and extending to an exit of the fining zone and rises uniformly from the depth of the substantially horizontal floor in the melting zone to a final depth that is at least 10 percent less than the depth of the substantially horizontal floor in the melting zone.

2. A submerged combustion melter comprising:

a floor, a roof, and a sidewall structure connecting the floor and roof defining an internal space, a first portion of the internal space comprising a melting zone, and a second portion of the internal space comprising a fining zone downstream of the melting zone, a third portion of the internal space comprising a treating zone downstream of the melting zone and upstream of the fining zone, the treating zone comprising one or more non-burner apparatus configured to inject a treating composition into a molten mass of glass containing bubbles in the treating zone, and a fourth portion of the internal space comprising a feed zone upstream of the melting zone, wherein the feed zone, the treating zone, and the fining zone are all devoid of submerged combustion burners and other apparatus that would increase turbulence above that in the melting zone;

one or more combustion burners in either the floor, the roof, the sidewall structure, or any two or more of these, producing combustion gases and configured to emit the combustion gases from a position under a level of, and positioned to transfer heat to and produce, a turbulent molten mass of glass containing bubbles in the melting zone;

a skimmer having distal end adapted to extend to a point just above a level of molten mass of glass exiting the fining zone to hold back a portion of foam floating on the molten mass of glass flowing out of the fining zone; and

the submerged combustion melter comprising a geometry whereby the level of the molten glass is substantially equivalent in the feed zone, the melting zone, the treating zone, and the fining zone, wherein the floor in the melting zone is substantially horizontal, the floor in the feed zone is angled at an angle β

with respect to the substantially horizontal floor in the melting zone so that the floor in the feed zone falls uniformly from an initial depth that is at least 10 percent less than a depth of the substantially horizontal floor in the melting zone, and the floor in the fining zone is angled at an angle α

with respect to the substantially horizontal floor in the melting zone so that the floor in the fining zone is angled upward relative to horizontal beginning at an entrance to the fining zone and extending to an exit of the fining zone and rises uniformly from the depth of the substantially horizontal floor in the melting zone to a final depth that is at least 10 percent less than the depth of the substantially horizontal floor in the melting zone, and α and

β

are the same or different.

3. A process comprising:

charging a feed composition into a submerged combustion melter comprising a geometry, at least a portion of the feed composition comprising a vitrifiable material;

heating the feed composition with one or more submerged combustion burners, thereby melting at least a portion of the vitrifiable material in a melting zone of the submerged combustion melter to form a turbulent molten mass of glass and bubbles in the melting zone;

allowing the turbulent molten mass of glass and bubbles to flow from the melting zone into a treating zone devoid of submerged combustion burners and other apparatus or components that would increase turbulence above that in the melting zone, thus forming a less turbulent molten mass of glass containing bubbles in the treating zone, the treating zone immediately downstream of the melting zone, while injecting a treating composition into the less turbulent molten mass of glass containing bubbles in the treating zone using one or more non-burner apparatus, thus forming a treated molten mass of glass having foam on an upper surface thereof;

allowing the treated molten mass of glass and bubbles to flow into a fining zone in the submerged combustion melter immediately downstream of the treating zone, the fining zone devoid of submerged combustion burners and other apparatus or components that would increase turbulence above that in the melting zone and the treating zone, thus forming a fined molten mass of glass having foam on an upper surface thereof;

skimming at least a portion of the foam on the upper surface of the fined molten mass of glass as it leaves the fining zone; and

maintaining a level of molten glass in the treating zone and the fining zone substantially equal to a level of the molten glass in the melting zone, the melter geometry comprises a floor in the melting zone being substantially horizontal and a floor in the fining zone is angled upward at an angle α

with respect to the substantially horizontal floor in the melting zone so that the floor in the fining zone is angled upward relative to horizontal beginning at an entrance to the fining zone and extending to an exit of the fining zone and rises uniformly from the depth of the substantially horizontal floor in the melting zone to a final depth that is at least 10 percent less than the depth of the substantially horizontal floor in the melting zone.

4. The process of claim 3 comprising flowing the fined molten mass of glass from the fining zone into a flow channel fluidly and mechanically connected to the melter downstream of the fining zone.

5. The process of claim 3 wherein the skimming of at least a portion of the foam on the upper surface of the fined molten mass of glass as it exits the fining zone comprises using a skimmer having a distal end, the distal end extending into the molten glass a depth sufficient to hold back a portion of the fined molten mass of glass flowing out of the submerged combustion melter through an exit that is lower than the distal end of the skimmer.

6. The process of claim 3 comprising decreasing stability of the bubbles using the treating composition.

7. The process of claim 6 wherein the treating composition is selected from the group consisting of nitrogen, argon, dry air, nitrogen-enriched dry air, and combinations thereof.

8. The process of claim 3 comprising increasing stability of the bubbles using the treating composition.

9. The process of claim 8 wherein the treatment composition is selected from the group consisting of oxides of sulfur, oxides of nitrogen, and combinations thereof.

10. The process of claim 3 wherein the charging of a feed composition into a submerged combustion melter comprising a geometry comprises feeding a feed zone upstream of the melting zone, the feed zone devoid of submerged combustion burners.

11. The process of claim 3 comprising exhausting the submerged combustion melter employing an exhaust stack positioned in the roof of the fining zone.

12. A process comprising:

charging a feed composition into a feed zone of a submerged combustion melter, at least a portion of the feed composition comprising a vitrifiable material;

heating the feed composition with one or more submerged combustion burners, thereby melting at least a portion of the vitrifiable material in a melting zone of the submerged combustion melter immediately downstream of the feed zone to form a turbulent molten mass of glass and bubbles in the melting zone;

allowing the turbulent molten mass of glass and bubbles to flow from the melting zone into a treating zone devoid of submerged combustion burners and other apparatus or components that would increase turbulence above that in the melting zone, thus forming a less turbulent molten mass of glass containing bubbles in the treating zone, the treating zone immediately downstream of the melting zone, while injecting a treating composition into the less turbulent molten mass of glass containing bubbles in the treating zone using one or more non-burner apparatus, thus forming a treated molten mass of glass containing bubbles having foam on an upper surface thereof;

allowing the treated molten mass of glass containing bubbles having foam on the upper surface thereof to flow into a fining zone in the submerged combustion melter immediately downstream of the treating zone, the fining zone devoid of submerged combustion burners and other apparatus or components that would increase turbulence above that in the melting zone and the treating zone, thus forming a fined molten mass of glass having foam on an upper surface thereof;

skimming at least a portion of the foam on the upper surface of the fined molten mass of glass as it leaves the fining zone; and

maintaining a level of molten glass in the feed zone, the treating zone, and the fining zone substantially equal to a level of the molten glass in the melting zone, wherein a floor in the melting zone is substantially horizontal, a floor in the feed zone is angled at an angle β

with respect to the floor in the melting zone so that the floor in the feed zone falls uniformly from an initial depth that is at least 10 percent less than a depth of the substantially horizontal floor in the melting zone, and a floor in the fining zone is angled at an angle α

with respect to the substantially horizontal floor in the melting zone so that the floor in the fining zone is angled upward relative to horizontal beginning at an entrance to the fining zone and extending to an exit of the fining zone and rises uniformly from the depth of the substantially horizontal floor in the melting zone to a final depth that is at least 10 percent less than the depth of the substantially horizontal floor in the melting zone, and α and

β

are the same or different.

13. The process of claim 12 comprising flowing the fined molten glass from the fining zone into a flow channel fluidly and mechanically connected to the melter downstream of the fining zone.

14. The process of claim 12 wherein the skimming of the fined molten mass of glass as it exits the fining zone comprises using a skimmer having a distal end, the distal end extending into the molten glass a depth sufficient to hold back a portion of the fined molten glass flowing out of the submerged combustion melter through an exit that is lower than the distal end of the skimmer.