U.S. patents available from 1976 to present.
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Method and composition for utilizing lime-urea hydrates to simultaneously reduce NOx and SOx in combustion effluents

Patent 4731233 Issued on March 15, 1988. Estimated Expiration Date: Icon_subject January 9, 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

Urea reduction of NOx in combustion effluents
Patent #: 4208386
Issued on: 06/17/1980
Inventor: Arand ,   et al.

Urea reduction of NOx in fuel rich combustion effluents
Patent #: 4325924
Issued on: 04/20/1982
Inventor: Arand ,   et al.

Gas desulfurization
Patent #: 4424197
Issued on: 01/03/1984
Inventor: Powell ,   et al.

Process for removal of nitrogen oxides and sulfur oxides from waste gases
Patent #: 4442079
Issued on: 04/10/1984
Inventor: Donelly ,   et al.

Fluid bed SOX/NOX process--"hydrated calcine absorption"
Patent #: 4442080
Issued on: 04/10/1984
Inventor: Donnelly ,   et al.

Absorbent for the dry removal of sulfur dioxide and like components of an exhaust gas
Patent #: 4526703
Issued on: 07/02/1985
Inventor: Gebhard ,   et al.

Carboxylic acid activated dry calcium absorbent method for removing sulfur dioxide from a flue gas Patent #: 4533532
Issued on: 08/06/1985
Inventor: Gebhard ,   et al.

Inventors

Application

No. 06/817319 filed on 01/09/1986

US Classes:

423/239.1, Utilizing solid sorbent, catalyst, or reactant423/242.7, Amine423/243.08Alkali or alkali earth compound reactant

Examiners

Primary: Heller, Gregory A.
Assistant: Freeman, Lori S.

Attorney, Agent or Firm

International Class

B01D 53/60 (20060101)

Abstract

Methods and compositions are provided for simultaneous reduction of NOx and SOx in combustion effluents and process gas streams, employing a sorbent material of calcium or dolomitic lime hydrated with aqueous carboxamides, optionally with carbinol reductants, in amounts sufficient to reduce the NOx and SOx concentrations from the effluents. The sorbent material may be introduced as dry powders or wet hydrates in effluent streams at temperatures ranging from 400° to 2400° F.

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