Means and method for removing airborne particulates from an aerosol stream

• US 4,345,916 A
• Filed: 05/19/1980
• Issued: 08/24/1982
• Est. Priority Date: 05/19/1980
• Status: Expired due to Term

• Current Assignee: Marx Brook
• Original Assignee: Clyde N. Richards, Marx Brook
• Inventors: Richards, Clyde N., Brook, Marx
• Primary Examiner(s): Prunner, Kathleen J.
• Application Number:
  US06/151,352
• Time in Patent Office: 827 Days
• Field of Search: 55/5, 55/7-11, 55/83, 55/94, 55/107, 55/122, 55/135, 55/223, 55/226, 55/262-263, 261/DIG. 76, 261/17, 261/115, 261/DIG. 9, 261/DIG. 54
• US Class Current: 95/60
• CPC Class Codes: B01D 47/06 Spray cleaning
• CPC Class Codes: B03C 3/16 wet type
• CPC Class Codes: Y10S 261/09 Furnace gas scrubbers
• CPC Class Codes: Y10S 261/54 Venturi scrubbers
• CPC Class Codes: Y10S 261/76 Steam

Abstract

Disclosed herein is a method for removing airborne particulates from an aerosol stream by first humidifying said aerosol with steam, and then cooling said aerosol with water to saturation temperature. Thereafter, the saturated aerosol is adiabatically cooled to a supersaturated state and maintained at supersaturation for a time sufficient to permit the growth and removal thereof of said particulates. Further disclosed is an apparatus adapted for practicing the method of the present invention and employing charged droplet scrubbing techniques to remove said particulates.

Claims

1. A method for removing airborne particulates from an aerosol stream, comprising the steps of

(a) saturating said aerosol stream with water vapor;

(b) supersaturating said saturated aerosol stream for a time sufficient to permit condensation of said water vapor upon, and growth of said particulates; and

(c) scrubbing said supersaturated aerosol stream, while maintaining said stream at supersaturation, whereby to remove said particulates therefrom.

2. A method as set forth in claim 1 wherein the step of saturating said aerosol stream comprises the steps of:

(a) humidifying said aerosol stream with water vapor whereby to obtain an unsaturated aerosol stream having a predetermined mixing ratio; and

(b) cooling said humidified aerosol stream to saturation temperature.

3. A method as set forth in claim 2 wherein said aerosol stream is humidified by admixing steam therewith.

4. A method as set forth in claim 2 wherein said humidified aerosol stream is cooled to saturation temperature by passing said humidified aerosol stream through a mist of water.

5. A method as set forth in claim 1 wherein the step of supersaturating said saturated aerosol stream comprises adiabatically cooling said saturated aerosol stream by passing said saturated aerosol stream through a converging duct.

6. A method as set forth in claim 1 wherein at least a part of the particulates, prior to said condensation, have a diameter less than about one micron.

7. A method as set forth in claim 1 wherein said supersaturated aerosol is maintained at supersaturation for a time sufficient to grow said airborne particulates to a size of about 1.0 to 5.0 microns diameter.

8. A method as set forth in claim 1 wherein said supersaturated aerosol is maintained at supersaturation for about 0.1 seconds.

9. A method as set forth in claim 1 wherein the step of scrubbing said supersaturated aerosol stream comprises sweeping highly charged droplets of scrubbing liquor across the flow path of said supersaturated aerosol stream whereby to cause said highly charged droplets to collect said particulate from the aerosol stream.

10. A method as set forth in claim 9 wherein said scrubbing liquor is water.

11. A method as set forth in claim 10 wherein said highly charged droplets have a size of about 500 microns diameter.

12. A method as set forth in claim 1, further comprising the step of admixing NO_x and SO_x conditioning particulate with said aerosol stream prior to saturation thereof.

13. An apparatus for removing airborne particulates from an aerosol stream, comprising:

(a) means for saturating said aerosol stream with water vapor;

(b) means for supersaturating said saturated aerosol stream for a time sufficient to permit condensation of said water vapor upon, and growth of said particulates; and

(c) means for scrubbing said supersaturated aerosol stream, while maintaining said stream at supersaturation, whereby to remove said particulates therefrom.

14. An apparatus as set forth in claim 13 wherein said aerosol saturation means comprises:

(a) means for humidifying said aerosol stream with water vapor whereby to obtain an aerosol stream having a predetermined mixing ratio; and

(b) means for cooling said humidified aerosol stream to saturation temperature.

15. An apparatus as set forth in claim 14 wherein said means for humidifying said aerosol stream comprises a humidification vessel having aerosol stream inlet means, and outlet means at the opposite ends thereof for removing said aerosol, and means for controllably delivering steam into the interior of said vessel.

16. An apparatus as set forth in claim 14 wherein said means for cooling said humidified aerosol stream comprises a wash tower having inlet means at the base thereof for receiving said humidified aerosol stream and outlet means at the top for removing said saturated aerosol stream, and nozzle means within said tower for saturating said humidified aerosol stream with water vapor.

17. An apparatus as set forth in claim 13 wherein said supersaturation means comprises a converging duct.

18. An apparatus as set forth in claim 13 wherein said scrubbing means comprises highly charged droplets scrubbing means.