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

Co-disposal pollution control method

Patent 4726710 Issued on February 23, 1988. Estimated Expiration Date: Icon_subject June 16, 2006. 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

3859799

3876537

Sodium sulfur oxides wastes disposal process
Patent #: 3962080
Issued on: 06/08/1976
Inventor: Dulin ,   et al.

Process for insolubilizing potentially water pollutable wastes from sodium or ammonium type sulfur dioxide air pollution control systems
Patent #: 3984312
Issued on: 10/05/1976
Inventor: Dulin ,   et al.

Removal of sulfur oxides and particulate matter from waste gas streams
Patent #: 4004885
Issued on: 01/25/1977
Inventor: Groenendaal ,   et al.

Treatment of organic waste
Patent #: 4145396
Issued on: 03/20/1979
Inventor: Grantham

Process for flue gas desulfurization
Patent #: 4279873
Issued on: 07/21/1981
Inventor: Felsvang ,   et al.

Land restoration following oil-well drilling and products useful therefor
Patent #: 4353803
Issued on: 10/12/1982
Inventor: Dover, Jr.

Method for desulfurization and oxidation of carbonaceous fuels
Patent #: 4395975
Issued on: 08/02/1983
Inventor: Ashworth ,   et al.

Sealing system and method for sealing earthen containers
Patent #: 4439062
Issued on: 03/27/1984
Inventor: Kingsbury

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Inventors

Assignee

Application

No. 06/874622 filed on 06/16/1986

US Classes:

405/129.25, Chemical405/263Chemical

Examiners

Primary: Corbin, David H.

Attorney, Agent or Firm

International Classes

C04B 28/00 (20060101)
C04B 28/22 (20060101)

Abstract

Process for disposal of fossil fuel ash by addition thereto of sodium salts, preferably sodium sulfur oxide salt Na2 SOx where x is 3 and/or 4, in an amount ranging from 5-85 weight percent (dry basis) and adjusting the water percentage to within the range of 6-35%, preferably 15-28%. The coefficient of permeability of the ash and sodium salt is reduced from 102 cm/sec to the "impermeable" standard of 10-6 and below. The preferred mixes also call for a smectite clay additive present in the range of from 0.1% to 5%. A flocculant in amounts of 0.01% to 1% can be substituted for about 3-5% of the water content. A principal source of the Na2 SOx is sodium FGD waste, preferably from the use of Nahcolite (a natural mineral form of sodium bicarbonate) as an SOx sorbent in the Nahcolite FGD process. The resulting co-disposal process simultaneously renders the highly soluble Na2 SOx (102 g/L) and ash impermeable, and suitable for geomorphologically stable landfill disposal by known techniques to heights in excess of 200'.

Other References

  • Toxic and Hazardous Waste Disposal, vol. 1, Processes for Stabilization/Solidification, edited by Robert B. Pojasek, Ann Arbor Science Publishers Inc., 1979, chapter 18, pp. 363-399
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