U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Method and apparatus for separating out gall during glass melting processes

Patent 5683484 Issued on November 4, 1997. Estimated Expiration Date: Icon_subject December 18, 2015. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3208841

3294512

3362808

3375095

3385688

3482956

3573019

3592151

Method of melting a raw bath and a glass furnace for performing the method
Patent #: 4019888
Issued on: 04/26/1977
Inventor: Verhappen ,   et al.

Energy saving method of melting glass
Patent #: 4852118
Issued on: 07/25/1989
Inventor: Pieper

More ...

Inventors

Application

No. 574389 filed on 12/18/1995

US Classes:

65/134.5, By injecting gas below surface of molten glass65/134.8, By melting toxic or waste material65/327, At orifice65/347, MELTING POT OR FURNACE WITH STRUCTURALLY DEFINED DELIVERY OR FINING ZONE588/254, Contains asbestos588/256, Waste contains heavy metal (e.g., fly, ash, flue dust, and incinerator ash)588/900APPARATUS

Examiners

Primary: Czaja, Donald E.
Assistant: Vincent, Sean

Attorney, Agent or Firm

Foreign Patent References

  • OS 14711842 DE. 08/13/1970
  • 3912311 DE. 08/13/1990
  • WO 93/02974 WO. 02/13/1993

International Class

C03C 005/193

Foreign Application Priority Data

1994-12-25 DE

Abstract

An electrically heated tank furnace is used to melt glass whereby a floating gall layer is formed on the melt, in particular during the vitrification of hazardous materials such as asbestos, fly ash, filter dust, whereby the tank of the furnace is fitted with a discharge outlet for the melt and an overflow channel with an inlet for the gall. A stream of ascending gas bubbles is produced in the melt. In order to promote better and automatic draining of the gall the stream of gas bubbles is produced directly in front of the overflow channel which thereby maintains a layer of liquid gall in the overflow channel and a layer of molten glass retained by a weir on the bottom of the overflow channel. The temperature in the overflow channel is chosen to be above the melting temperature of the gall, whilst the bottom layer of glass is maintained at a temperature at which the viscosity of the glass is so high that the glass does not drain out the overflow channel.

Other References

  • Publication by Von G. Mayer-Schwinning, et al, entitled "Vitrification Process for the inertization of residual Products During Noxious Gas Removal in Termal Waste Disposal Units", VGB Kraftwerkstechnik 70 (1990) Issue 4, pp. 332-336
  • Publication by L. Penberty-Fred scarfe entitled "Electric Boosting and Bubbling for Glass Furnaces" date unknown
  • Publication by Pircus entitled "Melting Furnace Design in the Glass Industry" published by Books for Industry and the Glass Industry Magazine, dated 1980
  • Dr-Ing Hans-Joachin Illig, ABC Glas, Deutscher Verlag fur Grundstoffindustrie Leipzig, 1991--pp. 7, 9
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