U.S. patents available from 1976 to present.
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Process for vitrifying environmentally hazardous waste material in a glass melting furnace

Patent 5035735 Issued on July 30, 1991. Estimated Expiration Date: Icon_subject December 13, 2009. 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

Method of and apparatus for controlling batch thickness and glass level in a glass furnace
Patent #: 4312658
Issued on: 01/26/1982
Inventor: Mayer

Method for controlling the level of molten material in a furnace
Patent #: 4478628
Issued on: 10/23/1984
Inventor: Dunn

Hazardous waste removal method and apparatus
Patent #: 4632690
Issued on: 12/30/1986
Inventor: Colwell, Jr. ,   et al.

Purification of effluent gases
Patent #: 4652289
Issued on: 03/24/1987
Inventor: Drouet ,   et al.

Aqueous waste vitrification process and apparatus
Patent #: 4666490
Issued on: 05/19/1987
Inventor: Drake

Vitrification of asbestos waste
Patent #: 4678493
Issued on: 07/07/1987
Inventor: Roberts ,   et al.

Vitrification of asbestos waste
Patent #: 4820328
Issued on: 04/11/1989
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Process using melt accelerator for the conversion of solid waste substances into glass Patent #: 4944785
Issued on: 07/31/1990
Inventor: Sorg, et al.

Inventors

Assignee

Application

No. 450346 filed on 12/13/1989

US Classes:

65/134.8, By melting toxic or waste material65/27, Repairing or cleaning of apparatus; or batch dust prevention or control65/135.7, With submerged electrodes65/136.1, Preheating batch material65/136.4, By cooling molten glass405/129.5, Monitoring, detecting, or sensing405/129.55, Complete containment structure405/129.57, With drainage or collection501/155Composed of waste material

Examiners

Primary: Woodard, Joye L.

Attorney, Agent or Firm

International Class

C03B 005/16

Foreign Application Priority Data

1988-12-13 DE

Abstract

Process for vitrifying environmentally hazardous waste material in a glass melting furnace includes forming a batch including the waste material and no more than 30 weight percent additives including phonolite and SiO2 containing substances. A gall layer 2-5 cm thick including alkali salts or alkaline earth salts is produced on the molten glass, and batch is added so that a batch layer over 5 cm thick is formed on top of the gall layer. After the batch layer is formed, the molten glass is heated solely by electrodes, and the thickness of the batch layer is maintained to produce a steep enough temperature gradient therein so that the furnace atmosphere remains relatively cool, and substantially all of the condensable components which emerge from the molten glass condense in the batch layer.

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