Method for rapid induction heating of molten glass or the like

• US 4,780,121 A
• Filed: 04/03/1987
• Issued: 10/25/1988
• Est. Priority Date: 04/03/1987
• Status: Expired due to Fees

• Current Assignee: PPG Industries Incorporated (Nouryon BV)
• Original Assignee: PPG Industries Incorporated (Nouryon BV)
• Inventors: Matesa, Joseph M.
• Primary Examiner(s): LINDSAY JR, ROBERT
• Application Number:
  US07/033,944
• Time in Patent Office: 571 Days
• Field of Search: 65/134, 65/135, 65/335, 65/DIG. 4, 65/337, 65/27
• US Class Current: 62/134
• CPC Class Codes: C03B 2211/70 Skull melting, i.e. melting or refining in cooled wall crucibles or within solidified glass crust, e.g. in continuous walled vessels
• CPC Class Codes: C03B 5/00 Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
• CPC Class Codes: C03B 5/021 by induction heating
• CPC Class Codes: C03B 5/12 in shaft furnaces C03B5/02 takes precedence
• CPC Class Codes: C03B 5/225 Refining C03B5/18 takes precedence ; Refining agents C03C1/004
• CPC Class Codes: C03B 5/2252 under reduced pressure, e.g. with vacuum refiners
• CPC Class Codes: Y10S 65/04 Electric heat

Abstract

A melt of a material such as glass is inductively heated at a stage intermediate an initial liquefying stage and a refining stage. The function of the intermediate induction heating stage is essentially limited to raising the temperature of the melt a relatively minor amount to a refining temperature. Therefore, the induction heating stage may be compact with an intensified heating rate and rapid throughput, thereby permitting the induction heating zone to be a "cold" walled vessel without an appreciable effect on efficiency.

Claims

1. A method of melting and refining glass comprising:

providing a melt of unrefined glass at a first stage;

transferring the melt to a second stage comprising a metallic vessel of small volume relative to other stages of the process, holding a mass of the melt in the vessel less than 0.1 times the daily throughput of the process, cooling the metallic vessel by circulating coolant fluid in contact therewith sufficiently to maintain a solidified layer of the melt on the interior of the vessel, and electromagnetically inducing electric currents in the melt within the vessel by means of a coil around the metallic vessel to which is supplied high frequency alternating current to induce electric currents of at least 100 killowatts per cubic foot (3.5 kilowatts per liter) so as to rapidly raise the temperature of the melt to a refining temperature; and

after a resistance time in the second stage insufficient to significantly refine the melt, transferring the heated melt to a third stage where the melt is refined.

2. The method of claim 1 wherein the volume of melt held in the second stage vessel is less than 0.06 times the daily throughput of the process.

3. The method of claim 1 wherein the temperature of the melt is raised in the second stage 100°

F. (55°

C.) to 700°

F. (390°

C.).

4. The method of claim 1 wherein the average residence time of melt in the second stage is less than 10 minutes.

5. The method of claim 1 wherein the melt is subjected to sub-atmospheric pressure in the third stage.

6. The method of claim 1 wherein the glass is melted and refined at a rate of at least 10 tons per day.

7. The method of claim 6 wherein the glass is soda-lime-silica glass.

8. The method of claim 1 wherein the average residence time of melt in the second stage is less than five minutes.