Sonic cavitation and ozonation of waste material

• US 4,076,617 A
• Filed: 01/17/1977
• Issued: 02/28/1978
• Est. Priority Date: 04/22/1971
• Status: Expired due to Term

• Current Assignee: TII Corporation
• Original Assignee: TII Corporation
• Inventors: Stahl, Donald P., Furey, Richard F., Bybel, David
• Primary Examiner(s): Bascomb, Jr., Wilbur L.
• Assistant Examiner(s): Therkorn, Ernest G.
• Application Number:
  US05/760,005
• Time in Patent Office: 407 Days
• Field of Search: 210/19, 210/60, 210/61, 210/63 Z, 210/64, 210/150, 210/151, 210/188, 210/192, 210/194, 210/195 R, 210/199, 210/201, 210/202, 210/205, 210/218, 210/221 P, 210/252 , 210/259, 210/294, 210/320, 210/519, 21/54 A, 21/54 R, 21/58, 21/102 A, 259/DIG. 43, 259/DIG. 44, 261/81, 261/121 R, 261/123, 261/124, 261/DIG. 42, 261/DIG. 48
• US Class Current: 210/748.03
• CPC Class Codes: C02F 1/20 by degassing, i.e. liberation of dissolved gases degasification of liquids in general B01D19/00; arrangement of degassing apparatus in boiler feed supply F22D
• CPC Class Codes: C02F 1/36 ultrasonic vibrations
• CPC Class Codes: C02F 1/78 with ozone C02F1/4672 takes precedence
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: Y10S 261/42 Ozonizers
• CPC Class Codes: Y10S 261/48 Sonic vibrators

Abstract

Waste such as sewage or industrial effluent is emulsified by cavitation with acoustical energy and the emulsion is then ozonated to provide a purified product.

Claims

1. A process for combined acoustic treatment and ozonation of liquid waste material, comprising the steps of, placing the waste material in a vessel,

providing the vessel with diffusers that emit gaseous bubbles thereinto, said diffuser causing said bubbles to cover at least 90 percent of the cross-sectional area of the vessel so as to divide the vessel by a gaseous barrier into a generally lower acoustic treatment section with a generally upper ozone contact section,

initially placing said waste material into the acoustic treatment section, imparting acoustic energy to said material in said section at an energy level sufficient to cavitate and to emulsify said waste material,

transferring said cavitated liquid to said ozone contact section, and diffusing a gas stream containing 0.5 to 10% ozone into said ozone contact section.

2. A process as in claim 1, wherein said vessel is open to the atmosphere and said acoustic treatment and ozone contact sections are at atmospheric pressure.

3. A process as in claim 1, wherein said vessel is closed and said acoustic treatment and ozone contact sections are approximately at atmospheric pressure or slightly higher.

4. A process according to claim 3, wherein said cavitation emulsifies said waste material.

5. A process as in claim 3, wherein said diffusers have apertures therein, and said ozone containing gas is emitted from said apertures.

6. A process according to claim 3, wherein said acoustic energy is confined to said gaseous barrier and said lower level.

7. A process according to claim 6, wherein said vessel is open to the atmosphere and said upper and lower levels are at atmospheric pressure.

8. A process according to claim 6, wherein said vessel is closed and said diffusers project the gaseous bubbles in a generally upward direction.

9. A process according to claim 1, wherein said diffusers have apertures therein and said ozone containing gas is emitted from said apertures.

10. A process according to claim 9, wherein said ozone is bubbled through said upper level in a substantially uniform concentration thereacross.

11. A process according to claim 1, wherein the acoustic energy is produced as acoustic radiation with square wave shape.

12. A process according to claim 11, wherein the acoustic radiation with square wave shape is rich in harmonic oscillations and has little side lobe suppression.

13. A process according to claim 12, wherein the acoustic wave radiation is generated by a plurality of lead zirconate block transducers.

14. A process according to claim 13, wherein the power supplied to the transducers is between 500 and 1,000 kva with a frequency of 20 to 70 kc.

15. A process according to claim 1, wherein the acoustic treatment section for the waste water acts as a resonant circuit.

16. A process according to claim 1, which includes the steps of creating an emulsion of the waste material by the cavitation thereof, which emulsion is transferred to the ozone contact section so that during ozone contact, ozone in finely divided form is blown into the ozone contact section containing the emulsion so that it bubbles through the emulsion.

17. A process according to claim 1, wherein the waste material which is ozonated in the second process step is agitated and vented in a final step.

18. A process according to claim 17, wherein the ozonated waste material is passed through a free-fall spill chamber in order to agitate and vent it.