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

Acid rain abatement

Patent 5023063 Issued on June 11, 1991. Estimated Expiration Date: Icon_subject March 26, 2010. 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

Process for the treatment of sulfur and nitrogen oxides formed during power generation
Patent #: 4012488
Issued on: 03/15/1977
Inventor: Brocoff

Catalyst for reducing nitrogen oxides in a waste gas and a process for catalytically reducing nitrogen oxides contained in a waste gas
Patent #: 4182745
Issued on: 01/08/1980
Inventor: Nishida ,   et al.

Catalyst for selectively reducing nitrogen oxides from oxygen-containing exhaust gases
Patent #: 4282115
Issued on: 08/04/1981
Inventor: Atsukawa ,   et al.

Process for removing sulfur oxide and nitrogen oxide Patent #: 4830840
Issued on: 05/16/1989
Inventor: Bhattacharyya

Inventor

Assignee

Application

No. 498539 filed on 03/26/1990

US Classes:

423/239.1, Utilizing solid sorbent, catalyst, or reactant423/242.3, Organic acid423/576.5Transition metal-containing mixture

Examiners

Primary: Heller, Gregory A.

Attorney, Agent or Firm

International Classes

B01J 008/00
C01B 021/00
C01B 017/00

Abstract

The process of this invention will remove from acid rain essentially all of both the sulfur oxides (SOX) and nitrogen oxides (NOX) by catalytically reducing the NOX to water and elemental nitrogen and the SOX to either H2 S or elemental sulfur as desired. The process employs specific catalysts in the heteropoly acid or salt group and the spinel or inverse spinel group. The process conditions achieve an oxygen-free environment and reduction is effected with stoichiometric to 100% excess above stoichiometric H2 or H2 and CO as reducing gas. Temperatures can be 200° to 900° C. with the lower temperature range being favored; space velocity can be 2000 to 20,000 and still achieve 95+% abatement. The only product of the reaction which must be disposed of is saleable elemental sulfur.

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