Method of and apparatus for melting of glass

• US 4,029,489 A
• Filed: 02/17/1976
• Issued: 06/14/1977
• Est. Priority Date: 02/17/1976
• Status: Expired due to Term

• Current Assignee: Owens- Corning Fiberglas Technology Incorporated (Owens Corning)
• Original Assignee: Owens-Corning Fiberglas Corporation (Owens Corning)
• Inventors: Froberg, Magnus L., Hohman, Charles M.
• Primary Examiner(s): Kellogg, Arthur D.
• Application Number:
  US05/658,643
• Time in Patent Office: 483 Days
• Field of Search: 65/134, 65/135, 65/136, 65/337, 65/345, 65/347, 65/335
• US Class Current: 65/135.7
• CPC Class Codes: C03B 5/03 Tank furnaces
• CPC Class Codes: C03B 5/235 Heating the glass C03B5/02, C03B5/18, C03B5/225 take precedence

Abstract

A glass melting furnace in which glass can be heated by sources below its upper surface, as electrically by Joule effect, and by means above its upper surface, as by fossil fuel firing or by heat reflectors. A cold top melting mode is employed in the charging region of the furnace while the glass discharge region maintains an exposed molten, upper surface on the glass. In a disclosed embodiment a high crown over the charging region enables cold top melting and refining to be accomplished by Joule effect while flues and burner ports in that region are closed. A low crown, which may be adjustable in its height above the glass line, is provided over the discharge region to increase heating at the exposed, molten upper surface of the glass by reflection. Heating in the discharge region can be augmented by above surface heaters distributed across the crown. A flue in the discharge region carries gases from that region. The degree of heat flow from the discharge region to the charging region is controlled by an adjustable heat barrier. One form of barrier is a transverse wall mounted between the regions and arranged for adjustable elevation above the glass line. The degree of refinement of the glass in the discharge region permits use of the surface throat in furnaces where Joule effect heating provides the preponderant source of heat.

Claims

1. Apparatus for the melting and fining of glass comprising a receptacle for containing glass constituents including molten glass up to a glass line and glass batch above portions of said glass line;

a first region in said receptacle adapted to receive glass batch;

a second region in said receptacle spaced horizontally from said first region and adapted to have molten glass withdrawn therefrom;

a heat source beneath the glass line in said first and second regions adapted to heat the glass;

means for distributing glass batch as a blanket over a preponderance of the upper surface of said first region;

a heat source beneath the glass line adapted to heat the glass; and

a cover for said receptacle to enclose the space above said second region, said cover having a flue for the passage of gas from beneath said cover and said cover being positioned sufficiently close to said glass line so as to reflect heat from within the glass in said second region back to the exposed upper surface of the glass in said second region to increase the fluidity of said surface to an extent to facilitate the escape of gas from said surface in said second region while thermal conditions at the exposed surface of said first region maintain a batch blanket over a preponderance of the upper surface of said first region.

2. Apparatus according to claim 1 wherein said cover is spaced above said glass line of the order of inches.

3. Apparatus according to claim 1 wherein a source of heat energy is located between said cover and the upper surface of the glass constituents beneath said cover.

4. Apparatus according to claim 1 including mechanism to shift the location of said second cover vertically.

5. Apparatus according to claim 1 including a thermal barrier above the glass constituents in said receptacle and between said first region and said second region to inhibit the flow of heat from above said second region to above said first region.

6. Apparatus for the melting and fining of glass comprising a receptacle for containing molten glass up to a glass line and glass batch above said glass line;

means for introducing glass batch into said receptacle in a first region and for discharging molten glass from a second region spaced from the first region;

a first cover for said receptacle to enclose the space above said first region;

heaters beneath the glass line in said first and second regions adapted to heat said glass;

a second cover to enclose the space above the second region, said second cover having a flue for the passage of gas from beneath said second cover, said second cover being positioned less than half the height of the first cover above the glass line and being positioned sufficiently close to said glass line so as to reflect heat developed within said molten glass in said second region back to the exposed upper surface of glass in said second region and beneath said second cover to a sufficiently greater extent than heat is reflected back to the exposed upper surface of said first region to heat the surface of said glass in the second region to increase the fluidity of said surface to an extent to promote the escape of gas therefrom while the thermal conditions at the exposed surface of said first region maintain a batch blanket over a preponderance of the upper surface of said first region.

7. Apparatus according to claim 6 wherein said second cover is flat and generally parallel to the surface of the glass beneath it.

8. Apparatus according to claim 7 wherein said first cover is about six feet above the surface of the glass constituents beneath it, said second region has an upper surface about eight feet by about fourteen feet and said second cover is no more than about two feet from the surface of the glass beneath it.

9. Apparatus according to claim 6 wherein a source of heat energy is located between said second cover and the upper surface of the glass constrained beneath said second cover.

10. Apparatus according to claim 6 wherein said second cover has a burner port over said second region;

and a burner adapted to develop a swirl type flame is directed through said port to sweep the space between said second cover and the glass constrained beneath said second cover.

11. Apparatus according to claim 10 wherein said second cover is generally horizontal and the burner is oriented to develop a generally horizontal swirl.

12. Apparatus according to claim 6 including mechanism to shift the location of said second cover vertically.

13. Apparatus according to claim 6 wherein said second cover is oriented with its margin proximate said first end closer to said glass line than its margin proximate said discharge end.

14. Apparatus according to claim 13 wherein said second cover is of a heat reflective refractory of generally planar form inclined to the horizontal longitudinally of the furnace.

15. Apparatus according to claim 6 including a thermal barrier between said first region and said second region to inhibit the flow of heat from above said second region to above said first region;

and means to control the thermal barrier to control the amount of heat flow.

16. Apparatus according to claim 6 including a partition between said first and second covers extending generally vertically and transverse of a longitudinal axis between said ends of said tank, said partition having a lower margin above and closely adjacent the glass line.

17. Apparatus according to claim 16 including means to shift the elevation of the lower margin of said partition.

18. Apparatus according to claim 6 wherein the elevation of said first cover above said glass line is about three times the elevation of said second cover above said glass line.

19. Apparatus according to claim 6 wherein said first cover is crowned to about 6 feet above said glass line.

20. Apparatus according to claim 6 including a flue from said first region;

said sidewalls in said first region having a plurality of burner ports;

means to close said flue; and

means to close said burner ports.

21. Apparatus according to claim 6 wherein said second cover has a plurality of burner ports over said second region, and a burner for each port adapted to develop a swiry type flame directed to sweep the space between said second cover and the glass constrained beneath said second cover without direct impingement on said glass.

22. Apparatus according to claim 6 wherein the preponderant source of heat for glass in said first region is Joule effect heating developed through electrodes extending through the walls of said tank below said glass line;

wherein operating thermal conditions in said first region enable a blanket of batch to be maintained from side wall to side wall above molten glass in a layer extending from said first end wall essentially over said first region;

wherein operating thermal conditions in said second region enable a molten glass surface to be maintained from side wall to side wall from said discharge end wall essentially over said second region; and

a surface throat extending from said discharge end for withdrawing molten glass free of batch from said tank.

23. The method of operating a continuous glass melting and refining furnace which comprises the steps of applying a preponderance of the heat applied to a body of molten glass beneath the upper surface of that glass;

applying glass batch to the mass of glass constituents including the body of molten glass in a charging region remote from a withdrawal region and from a level above the molten glass;

distributing glass batch over a substantial portion of the upper surface of the body of molten glass;

withdrawing molten glass from the body of molten glass in the withdrawal region adjacent one side of the body;

maintaining a heat reflective surface in close proximity above the mass of glass constituents in the withdrawal region to reflect heat to the surface of the mass of glass constituents in thre withdrawal region beneath the heat reflective surface to an extent to maintain the upper surface of the mass of glass constituents beneath the heat reflective surface sufficiently fluid to promote the escape of gas therefrom, to maintain the upper surface essentially free of batch, and to define a leading edge of the batch blanket at its interface with an upper surface of the molten glass generally along the edge of the withdrawal region most proximate said charging region.

24. The method according to claim 23 wherein glass batch is fed from spaced stations along the wall of the tank constraining the glass constituents and is caused to flow across the body of molten glass from the spaced stations and toward the withdrawal region.

25. The method according to claim 23 wherein said heat is developed in the body of molten glass by Joule effect.

26. The method according to claim 23 wherein said substantial portion of the glass surface is about 80% of the upper surface.

27. The method according to claim 23 wherein the molten glass is withdrawn at the upper surface of the molten glass body.

28. The method according to claim 23 including the step of enclosing the upper surface of the mass of glass constituents in the charging region whereby gas currents and dust escape from the charging region are minimized.

29. The method according to claim 28 including the step of maintaining the enclosing surfaces above the batch blanket sufficiently remote from the batch blanket upper surface that the temperature in the major portion of the charging region is below that at which the glass batch melts.

30. The method according to claim 23 including the step of controlling the amount of heat transmitted from the withdrawal region of the charging region to melt at least a portion of the upper surface of batch along the leading edge of the batch blanket.

31. The method according to claim 30 wherein the controlling of transmitted heat is by the positioning of a heat barrier between the withdrawal region and the charging region.

32. The method according to claim 31 wherein the heat barrier is a wall having a lower edge positioned above the molten glass upper surface and including the step of adjusting the heat transmitted by adjusting the height of the lower edge of the barrier wall above the exposed, upper surface of the glass constituents.

33. The method according to claim 32 including the step of adding heat from a source other than the Joule effect heating of the molten glass to the withdrawal region from above the exposed upper surface of the glass constituents.

34. The method according to claim 23 including the step of venting the withdrawal region from above the upper surface of the molten glass.

35. The method according to claim 23 wherein the general temperature below the reflective surface and above the upper surface of glass constituents withdrawal region is about 2100°

F. and including the steps of enclosing the upper surface of the mass of glass constituents in the charging region and adjusting the heat transmitted from the withdrawal region to the charging region as a function of the height of the lower edge of the barrier wall in the relationship over the height range of one inch to two feet and a general temperature within the enclosure above the upper surface of glass constituents in the charging region in the range of about 500°

to 1340°

F. respectively.

36. The method according to claim 23 including the step of adjusting the amount of heat reflected to the upper surface of the glass constituents in the withdrawal region from the heat reflective surface.

37. The method according to claim 36 wherein the step of adjusting the amount of heat reflected includes adjusting the height of the reflective surface above the upper surface of the glass constituents.

38. The method according to claim 23 including the step of controlling the location of the leading edge of the batch blanket by positioning the heat reflective surface closer to the upper surface of the mass of glass constituents along the side of said heat reflective surface most proximate the charging region than along the side most remote from the charging region.

40. The method according to claim 34 wherein the barrier is a wall having a lower edge proximate the upper surface of the mass of glass constituents and wherein the step of adjusting involves adjusting the height of the lower edge of the wall above the upper surface of the mass of glass constituents.

39. The method of operating a continuous glass melting and refining furnace having a charge and discharge region wherein a batch blanket is maintained on the upper surface of the glass constituents in the charge region and the upper surface of the glass constituents in the discharge region is molten glass which comprises the steps of applying a preponderance of the heat applied in the charge and discharge regions to the mass of glass constituents by Joule effect;

augmenting the Joule effect heat with heat directed toward the upper surface of the glass mass in the discharge region from above that upper surface;

imposing a barrier to heat flow between the space above the discharge region and the space above the charge regions; and

adjusting the location of the leading edge of the batch blanket proximate to the discharge region by adjusting the flow of heat past the barrier from the space above the upper surface of the glass mass in the discharge region to the space above the upper surface of the glass in the charge region.