U.S. patents available from 1976 to present.
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Process and device for scrubbing flows of gaseous effluents loaded with polluting substances

Patent 5879432 Issued on March 9, 1999. Estimated Expiration Date: Icon_subject May 7, 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

2101555

2519296

2662607

3203110

3292346

3545180

3555785

3683591

3902874

Arrangement for ammonia feed in copying equipment
Patent #: 4212655
Issued on: 07/15/1980
Inventor: Degenhardt ,   et al.

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Inventors

Application

No. 836286 filed on 05/07/1997

US Classes:

95/114, With plural indirect heat transfer steps on solid sorbent or gaseous fluid mixture or constituent thereof95/116, Inorganic gas or liquid particle sorbed (e.g., vapor, mist, etc.)95/123, Hot sweep gas95/148, And regeneration96/122, With recovery or separation means for desorbing fluid96/126, With heat exchange means96/130, With means for regenerating solid sorbent96/144Gas contacting means

Examiners

Primary: Spitzer, Robert

Attorney, Agent or Firm

Foreign Patent References

  • 1607907 SU 11/25/1990

International Class

B01D 053/04

Foreign Application Priority Data

1995-09-07 FR

Abstract

A process and device for scrubbing flows of gaseous effluents loaded with polluting substances, wherein the effluents are caused to circulate through a device including an array of scrubber units (4a to 4n) juxtaposed in an enclosure (3), each containing materials adsorbing the substances. When the adsorbing load thereof is saturated and for the scrubber units (4) to regain the scrubbing capacity thereof, they are selectively and successively isolated by a mobile collector (8) during the time required for their desorption by heating and for the substances to be transferred by an auxiliary fluid (a fraction of the circulating effluents for example or a gas delivered selectively to the inlet of the scrubber unit to be desorbed by an auxiliary circuit), and the substances mixed with the auxiliary fluid are possibly transferred towards a reactor (10) suited for removing them. The process can be applied for concentrating and scrubbing of polluting substances such as VOCs or gas dehumidification.

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