U.S. patents available from 1976 to present.
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Processes and apparatus for removing acid gases from flue gas

Patent 5997823 Issued on December 7, 1999. Estimated Expiration Date: Icon_subject August 18, 2017. 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 of removing pollutants from exhaust gases
Patent #: 4548797
Issued on: 10/22/1985
Inventor: Sauer ,   et al.

Method for removing sulfur oxides from hot flue gases
Patent #: 4555390
Issued on: 11/26/1985
Inventor: Bhatia

Treatment of flue gas
Patent #: 4562054
Issued on: 12/31/1985
Inventor: Bhatia

Flue gas desulfurization process Patent #: 4604269
Issued on: 08/05/1986
Inventor: Yoon

Inventor

Assignee

Application

No. 912319 filed on 08/18/1997

US Classes:

422/169, Including means providing sequential purification stages422/143, Including specific wind box or particulate matter support grid422/145, And means providing flow of particulate matter into or out of reaction chamber422/168, Waste gas purifier422/171, Solid, extended surface, fluid contact type422/216Compact bed of particulate, fluid contact material and means providing gravity flow of material within bed

Examiners

Primary: Tran, Hien

Attorney, Agent or Firm

International Class

B01D 050/00

Abstract

Processes and apparatus for removing acid gases from hot flue gases utilizing a slurry consisting of water, calcium chloride and at least one absorbing agent selected from a group consisting of calcium oxides, magnesium oxides, calcium hydroxides, magnesium hydroxides, alkali metal oxides, alkali metal hydroxides, and alkali metal carbonates, introducing the slurry into the rising stream of hot flue gas to absorb the acid gas into the water and thereafter to react the absorbed acid gas with the absorption agent and thereafter to evaporate the water to produce dry solids comprising reaction products and unreacted absorption agents suspended in the flue gas. The calcium chloride reduces the water vapor pressure of the slurry to reduce the rate at which the water evaporates so as to increase the rate at which the acid gas is absorbed into the water before the water evaporates. The dry solids include relatively large, relatively small, and intermediate sized dry solids with the relatively large and intermediate dry solids being first removed from the flue gas, the relatively large sized dry solids being discharged as waste, and the intermediate sized dry solids being recycled for reuse in reacting with the acid gas and with the relatively small sized dry solids being removed second from the flue gas and the relatively small sized dry solids recycled for reuse in reaction with the acid gases.

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