Multi-stage process and apparatus for refining glass or the like

• US 4,798,616 A
• Filed: 08/31/1987
• Issued: 01/17/1989
• Est. Priority Date: 10/02/1986
• Status: Expired due to Fees

• Current Assignee: PPG Industries Incorporated (Nouryon BV)
• Original Assignee: PPG Industries Incorporated (Nouryon BV)
• Inventors: Haskins, David R., Knavish, Leonard A.
• Primary Examiner(s): Kellogg, Arthur
• Application Number:
  US07/091,178
• Time in Patent Office: 505 Days
• Field of Search: 65/134, 65/135, 65/136, 65/337, 65/346, 65/347
• US Class Current: 65/135.8
• CPC Class Codes: C03B 3/02 combined with preheating, premelting or pretreating the glass-making ingredients, pellets or cullet
• CPC Class Codes: C03B 5/03 Tank furnaces
• CPC Class Codes: C03B 5/04 in tank furnaces C03B5/02 takes precedence
• CPC Class Codes: C03B 5/185 Electric means

Abstract

In a method of making glass or the like, wherein the batch materials are liquefied in a distinct zone from the refiner, the liquefied material is heated in an intermediate stage before being fed to the refiner. In preferred embodiments the intermediate stage comprises one or more channels extending from the side of the refiner.

Claims

1. In a method of making glass or the like wherein batch material is liquefied in a first vessel from which the liquefied material flows in an incompletely melted condition and is passed to a separate refiner vessel in which a volume of the material is gathered and heated so as to refine the material, and the refined material is withdrawn from an outlet at one end of the refiner, the improvement comprising receiving the incompletely melted material from the liquefying vessel in an intermediate vessel, heating the material in the intermediate vessel so that the material is passed from the intermediate vessel to the refiner at a temperature between the highest and lowest temperatures of the material in the refiner, maintaining a high temperature zone of the material in the refiner at a location between the outlet and an opposite rear end, maintaining a decreasing temperature gradient between the high temperature zone and the rear end so as to induce a rearward surface flow of material from the high temperature zone toward the rear end thereby establishing a horizontally elongated recirculating flow pattern that serves to extend the residence time of the material in the refiner, passing the material from the intermediate vessel into the refiner at a location between the high temperature zone and the rear end so as to enter directly into the rearward surface flow.

2. The method of claim 1 wherein the material flows from the intermediate vessel to the refiner vessel in a direction transverse to the rearward surface flow.

3. The method of claim 1 wherein a substantially greater volume of material is retained in the refiner vessel than in the intermediate vessel.

4. The method of claim 1 wherein the material is liquefied at two or more locations and passed to the refiner by way of two or more respective intermediate vessels.

5. The method of claim 1 wherein surface flow of low density material from the intermediate vessel is blocked.

6. The method of claim 1 wherein soda-lime-silica glass is being produced and the temperature of the material is raised in the intermediate vessel to within 200°

F. to 500°

F. of the peak temperature attained by the glass within the refiner vessel.

7. A method of making glass or the like comprising liquefying batch material and permitting the liquefied material to flow freely from the liquefying zone before it has completely melted, receiving the liquefied material in a horizontally extending channel of relatively narrow width where its temperature is increased, passing the material to a relatively wide refining vessel where its temperature is increased further, withdrawing refined molten material from an outlet end of the refining vessel, and the material entering the refining vessel from the channel is at a temperature compatible with joining a flow stream in the refining vessel that initially flows in a direction substantially away from the outlet end.

8. The method of claim 7 wherein material from the channel enters a side portion of the refining vessel.

9. The method of claim 8 wherein the material from the channel enters the refining vessel at 200°

F. to 500°

F. below the maximum temperature attained by the material in the refining vessel.

10. The method of claim 9 wherein the glass is a soda-lime-silica flat glass.

11. Apparatus for making glass or the like comprising:

a liquefying vessel having means for feeding pulverulent batch material into the vessel, means for heating the interior of the vessel to a liquefying temperature of the batch material, and a batch support surface extending to a drain opening;

a channel aligned with the drain opening adapted to receive liquefied material from the liquefying vessel, means for heating the liquefied material in the channel;

a refining vessel communicating with the channel so as to receive molten material from the channel, the refining vessel having a substantially greater area than the channel, means for heating the material in the refining vessel adapted to provide a relatively high temperature zone in a portion of the material in the refiner, and an outlet opening for withdrawing molten material from the refining vessel at a location spaced from the channel;

wherein the refining vessel has a longitudinal dimension extending horizontally from a back wall toward the outlet opening with side walls extending substantially in the longitudinal direction, and the channel communications with the interior of the refining vessel through an opening in a side wall portion between the back wall and the high temperature zone.

12. The apparatus of claim 11 wherein the channel extends transversely to the longitudinal dimension of the refining vessel.

13. The apparatus of claim 11 wherein at least two liquefying vessels and at least two channels are associated with the refining vessel.

14. The apparatus of claim 11 wherein the opening from the channel to the refiner is above the bottom of the refiner at that region.

15. The apparatus of claim 11 wherein the channel is provided with electric heating means.

16. The apparatus of claim 11 wherein the channel provides a passageway for molten material from the liquefying vessel to the refining vessel that is greater in length than in width.

17. The apparatus of claim 11 wherein the side wall opening is spaced from the back wall at least one fourth of the longitudinal dimension of the refining vessel.

18. The apparatus of claim 14 wherein the channel at its end near the opening onto the refiner is provided with barrier means for preventing surface flow of low density material through the opening.