U.S. patents available from 1976 to present.
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Process for desulfurizing Claus tail-gas

Patent 5229091 Issued on July 20, 1993. Estimated Expiration Date: Icon_subject April 15, 2012. 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

3764665

3821110

Process for simultaneously removing nitrogen oxides, sulfur oxides, and particulates
Patent #: 4692318
Issued on: 09/08/1987
Inventor: Tolpin ,   et al.

Process for removing sulfur oxides from a gas by means of an absorption mass regenerable by reaction with elemental sulfur
Patent #: 4855117
Issued on: 08/08/1989
Inventor: Deschamps ,   et al.

Process for the reduction of the sulfur content in a gaseous stream Patent #: 4857297
Issued on: 08/15/1989
Inventor: Kettner ,   et al.

Inventors

Assignee

Application

No. 868432 filed on 04/15/1992

US Classes:

423/244.01, Utilizing solid reactant or catalyst to remove or modify sulfur or sulfur containing component423/574.1With sulfur dioxide

Examiners

Primary: Heller, Gregory A.

Attorney, Agent or Firm

International Classes

B01J 008/00
C01B 017/00

Abstract

A process is disclosed for removing sulfur from tail-gas emitted from a Claus sulfur recovery process. First, the tail-gas is oxidized so as to convert sulfur therein to sulfur oxides. Oxidized tail-gas is directed into an absorber where a solid absorbent absorbs substantially all the sulfur oxides thereon. After allowing sufficient time for a desired amount of sulfur oxides to be absorbed, absorption is ceased. Next, the solid absorbent containing the absorbed sulfur oxides is contacted with a reducing gas so as to release an off gas containing hydrogen sulfide and sulfur dioxide. Upon releasing sulfur from the solid absorbent, the solid absorbent is regenerated and redirected into the absorber. Sulfur in the off gas emitted by regeneration is concentrated to an extent sufficient for use within a Claus sulfur recovery process for conversion to elemental sulfur. By combining this process with a Claus sulfur recovery process, sulfur dioxide emissions can be reduced to less than about two parts per million.

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