Charged droplet gas scrubber apparatus and method

• US 6,156,098 A
• Filed: 02/10/1999
• Issued: 12/05/2000
• Est. Priority Date: 02/10/1999
• Status: Expired due to Term

• Current Assignee: Clyde N. Richards
• Original Assignee: Clyde N. Richards
• Inventors: Richards, Clyde N.
• Primary Examiner(s): Chiesa, Richard L.
• Application Number:
  US09/248,013
• Time in Patent Office: 664 Days
• Field of Search: 95/64, 95/65, 95/71, 95/78, 95/70, 96/27, 96/52, 96/53, 96/55, 239/690.1
• US Class Current: 95/65
• CPC Class Codes: B01D 53/32 by electrical effects other than those provided for in group B01D61/00
• CPC Class Codes: B01D 53/78 with gas-liquid contact
• CPC Class Codes: B03C 3/16 wet type
• CPC Class Codes: B03C 3/41 Ionising-electrodes

Abstract

Gas scrubbing apparatus and method, employing highly charged liquid droplets for removal of both particulates and pollutant gases from the gas to be cleaned, allowing scrubbing of uncharged particulates by means of monopole--dipole attractive forces between the charged liquid droplets and the electric dipoles induced in the uncharged particulates by the charged droplets; employing electrode geometry at the site of droplet production and charging, having spreading liquid sheet electrodes emitting the droplets from the edges of the liquid sheets, interspersed with electrically conductive induction electrodes, with electrostatic potential of no more than about 20 kv existing between the induction electrode array and the array of liquid sheets, and with spacing such that adequately high electric field strength can be maintained at the edges of the liquid sheets to allow adequate charging of the droplets emitted from the liquid sheets, without the occurrence of corona discharges which could deplete droplet charges or interfere with production of the electric field strength required for adequate droplet charging; allowing the particulate and pollutant gas scrubbing procedures to be carried out simultaneously in a single chamber; requiring no substantial power other than that for the blower or other means which moves the gas to be cleaned through the cleaning chamber; and allowing these results to be achieved with low liquid-to-gas flow ratios.

Claims

1. Apparatus for removing both particulate pollutants and gaseous pollutants, from a gas to be cleaned, said gas to be cleaned already flowing in an established gas flow stream and gas flow direction upon entry into said apparatus, said gas flow direction defining a downstream direction in said gas flow stream as a direction parallel to said gas flow direction and defining an upstream direction in said gas flow stream as a direction opposite to said gas flow direction, said apparatus comprising:

(a) a pressurized liquid means, being a source providing a pressurized liquid at a controllable liquid pressure;

(b) a droplet production means, connected to said pressurized liquid means, for emitting copious quantities of droplets of said liquid;

(c) a droplet charging means, communicating with said droplet production means, for exposing said droplets, at the instant of emission of each of said droplets from said droplet production means, to an electric field of strength sufficient for charging said droplets to an average charge which is at least an appreciable portion of the maximum charge which may be carried by said droplets of said liquid;

(d) an injection means, acting upon said droplets, for injection of said droplets into said gas to be cleaned, and for intimately mixing said droplets with said gas to be cleaned by causing said droplets to travel through said gas to be cleaned in motion of said droplets through a length of travel relative to said gas to be cleaned; and

(e) a droplet removal means, communicating with said gas to be cleaned and said droplets injected into said gas, for removing said droplets from said gas to be cleaned after said droplets have interacted with said gas, and for collecting together said liquid contained in said droplets

wherein said pressurized liquid means, said droplet production means, said droplet charging means, and said injection means are so configured and operated as to provide said droplets with a combination of size, charge, droplet production rate, and length of travel of said droplets in said gas to be cleaned such as to cause removal of said pollutants with a desired particulate removal efficiency for said particulate pollutants, and to also cause removal of said gaseous pollutants with a desired gaseous pollutant removal efficiency.

2. Apparatus of claim 1, for use with a gas to be cleaned containing electrically charged particulates having a particulate charge polarity prior to entry into said apparatus, wherein said droplet charging means produces droplets having a charge polarity opposite to said particulate charge polarity.

3. Apparatus of claim 1, wherein said gas flow direction is vertical.

4. Apparatus of claim 3, wherein said gas flow direction is vertically downward.

5. Apparatus of claim 1, wherein said gas flow direction is horizontal.

6. Apparatus of claim 1, wherein said droplet production means and said injection means cause said droplets to be injected into said gas to be cleaned in said downstream direction.

7. Apparatus of claim 1, wherein said droplet production means and said injection means cause said droplets to be injected into said gas to be cleaned in said upstream direction.

8. Apparatus of claim 1, wherein said droplet removal means comprises an impingement separator.

9. Apparatus of claim 1, wherein said droplet removal means further comprises a mist eliminator.

10. Apparatus of claim 1, wherein said droplet removal means comprises an electrostatic precipitator.

11. Apparatus of claim 1, further comprising a recirculation means, connected to said droplet removal means and to said pressurized liquid means, for recirculating back to said pressurized liquid means, said liquid collected from said droplets by said droplet removal means.

12. Apparatus of claim 11, wherein said recirculation means comprises a flow line containing a pump and a strainer means for straining said liquid.

13. Apparatus of claim 1, wherein said droplets have a diameter in the range from 25 microns to 250 microns.

14. Apparatus of claim 13, wherein said droplets have a diameter substantially equal to 140 microns.

15. Apparatus of claim 13, wherein said droplets are injected into said gas to be cleaned with an average electric charge having a magnitude in the range from 0.1 to 2.0 times ten million elementary charge units.

16. Apparatus of claim 1, wherein said droplet production means comprises a means for producing a plurality of parallel spreading liquid sheet electrodes of a conductive liquid, each having a principal flow direction parallel to said gas flow direction, said sheets having edges emitting said droplets, and wherein said droplet charging means communicates electrostatically with said droplet production means.

17. Apparatus of claim 16, wherein said droplet charging means comprises, in combination with said spreading liquid sheet electrodes, a plurality of parallel induction electrodes, parallel to said gas flow direction, and a high voltage means, connected to said induction electrodes, for creating a high voltage between said induction electrodes and said spreading liquid sheet electrodes.

18. Apparatus of claim 17, wherein said spreading liquid sheet electrodes and said induction electrodes each lie on at least substantially equally spaced parallel planes, with the plane of each of said spreading liquid sheet electrodes being at least substantially equally spaced between the planes of the adjacent induction electrodes, and wherein said induction electrodes are located, at least in principal part, downstream from said edges of said spreading liquid sheet electrodes, but in which said edge of each of said spreading liquid sheet electrodes is located at least substantially between said adjacent induction electrodes.

19. Apparatus of claim 18, in which said voltage between said induction electrodes and said spreading liquid sheet electrodes is in the range from 10 KV to 20 KV, and in which the spacing between planes of adjacent induction electrodes and spreading liquid sheet electrodes is substantially equal to one inch;

and in which the flow rate of said liquid into said droplet production means is in the range from 10 to 30 gallons per minute per 1000 CFM of flow rate of said gas to be cleaned; and

in which said pressurized liquid means provides said liquid at a pressure in the range from 30 p.s.i. to 100 p.s.i.; and

in which said droplets have an average diameter in the range from 25 to 150 microns, and have an average electric charge having a magnitude in the range from 0.1 to 2.0 times ten million elementary charge units; and

in which said length of travel of said droplets relative to said gas is at least 0.5 meters.

20. Apparatus of claim 18, in which said voltage between said induction electrodes and said spreading liquid sheet electrodes is substantially equal to 17 KV, and in which the spacing between planes of adjacent induction electrodes and spreading liquid sheet electrodes is substantially equal to one inch.

21. Apparatus of claim 18, in which the flow rate of said liquid into said droplet production means is substantially 17 gallons per minute per 1000 CFM of flow rate of said gas to be cleaned.

22. Apparatus of claim 18, in which said droplets have an average diameter substantially equal to 140 microns.

23. Apparatus of claim 18, in which said droplets have an average electric charge having a magnitude substantially equal to ten million elementary charge units.

24. Apparatus of claim 18, in which said length of travel of said droplets relative to said gas is at least 0.5 meters.

25. Apparatus of claim 18, in which said voltage between said induction electrodes and said spreading liquid sheet electrodes is substantially equal to 17 KV, and in which the spacing between planes of adjacent induction electrodes and spreading liquid sheet electrodes is substantially equal to one inch;

and in which the flow rate of said liquid into said droplet production means is substantially 17 gallons per minute per 1000 CFM of flow rate of said gas to be cleaned; and

in which said droplets have an average diameter substantially equal to 140 microns; and

in which said droplets have an average electric charge having a magnitude substantially equal to ten million elementary charge units; and

in which said length of travel of said droplets relative to said gas is substantially equal to one meter.

26. Apparatus of claim 1, wherein said particulate removal efficiency is at least 90 per cent.

27. Apparatus of claim 1, wherein said particulate removal efficiency is at least 99 per cent.

28. Apparatus of claim 1, wherein said gaseous pollutant removal efficiency is at least 90 per cent.

29. Apparatus of claim 1, wherein said gaseous pollutant removal efficiency is at least 99 per cent.

30. Method for removing both particulate pollutants and gaseous pollutants, from a gas to be cleaned, said gas to be cleaned already flowing in an established gas flow stream and gas flow direction prior to application of said method, said gas flow direction defining a downstream direction in said gas flow stream as a direction parallel to said gas flow direction and defining an upstream direction in said gas flow stream as a direction opposite to said gas flow direction, said method comprising the steps of:

(a) Producing copious quantities of liquid droplets;

(b) Exposing said produced droplets, at the instant of emission of each of said produced droplets, to an electric field of strength sufficient for charging said droplets to an average electric charge which is at least an appreciable portion of the maximum charge which may be carried by said droplets of said liquid;

(c) Injecting said charged droplets into said gas flow stream of said gas to be cleaned in a manner causing said droplets to be intimately mixed with said gas to be cleaned by causing said droplets to travel through said gas to be cleaned in motion of said droplets through a length of travel relative to said gas to be cleaned; and

(d) removing said droplets from said gas to be cleaned after said droplets have interacted with said gas to be cleaned;

said method providing said droplets with a combination of size, charge, droplet production rate, and length of travel of said droplets in said gas to be cleaned such as to cause removal of said pollutants with a desired particulate removal efficiency for said particulate pollutants, and to also cause removal of said gaseous pollutants with a desired gaseous pollutant removal efficiency.

31. Method of claim 30, wherein said droplets have an average diameter in the range from 25 to 250 microns, and have an average electric charge having a magnitude in the range from 0.1 to 2.0 times ten million elementary charge units.