Method and apparatus for waste digestion using multiple biological processes

• US 5,626,755 A
• Filed: 11/08/1995
• Issued: 05/06/1997
• Est. Priority Date: 11/08/1995
• Status: Expired due to Term

• Current Assignee: Daniel R. Miklos
• Original Assignee: Micronair, Inc.
• Inventors: Holcombe, Don M., Keyser, Gene E.
• Primary Examiner(s): McCarthy, Neil
• Assistant Examiner(s): GREEN, THEODORE
• Application Number:
  US08/555,153
• Time in Patent Office: 545 Days
• Field of Search: 210/614, 210/620, 210/623, 210/626, 210/628, 210/630, 210/96.1, 210/101, 210/143, 210/150, 210/151, 210/195.1, 210/198.1, 210/202, 210/205, 210/209, 210/903, 210/22 0
• US Class Current: 210/614
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/201 Perforated, resilient plastic diffusers, e.g. membranes, sheets, foils, tubes, hoses
• CPC Class Codes: C02F 3/301 Aerobic and anaerobic treatment in the same reactor
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

Methods and apparatus for treating waste streams utilize controlled introduction of microscopic gaseous bubbles to create, in a single vessel, as many as three separate biological environments in discrete, stratified zones. In preferred embodiments, bubbles of air are introduced at the bottom of the vessel, creating an aerobic zone in this vicinity. Depletion of oxygen by microorganisms resident in this layer creates an anoxic zone that drifts upward, establishing itself above the aerobic layer. The two layers remain segregated due to the intolerance of aerobic microorganisms for the overlying anoxic environment, the sharpness of the interface depending on the degree of intolerance. Preferably, the treatment vessel is used in conjunction with a clarifier in an internal recycle configuration; clear water from the top of the clarifier is conducted away from the system as treated effluent, while a portion of the biomass settling at the bottom of the clarifier is returned to the head of the treatment vessel through a hydrocyclone and screen arrangement to remove inert content, thereby substantially increasing the efficiency of biological waste-digestion processes.

Claims

1. A method of treating liquid-borne waste containing at least two different types of waste-digestive microorganism, the different types of microorganism requiring mutually incompatible chemical environments and comprising an aerobic and a non-aerobic species, the method comprising:

a. introducing the waste into a treatment vessel having a bottom region;

b. continuously introducing a supply of micronized air bubbles into the bottom region of the waste-containing treatment vessel, the continuous supply of air bubbles corresponding to a quantity of introduced air thereby creating in the bottom region an aerobic zone compatible with and containing the aerobic species;

c. controlling the quantity of introduced air and the degree of agitation of the waste so as to produce in the waste at least one distinct non-aerobic zone vertically adjacent to the aerobic zone having a chemical environment compatible with and containing the non-aerobic species, thereby effecting biodegradation of the waste.

2. The method of claim 1 wherein the bubbles possess at least one of (a) stored potential energies of at least 10 lbm/ft² -sec² ;

and (b) work/area factors of at least 0.5 lbf/ft.

3. The method of claim 2 wherein the bubbles possess stored potential energies of at least 100 lbm/ft² -sec².

4. The method of claim 2 wherein the bubbles possess stored potential energies of at least 500 lbm/ft² -sec².

5. The method of claim 2 wherein the bubbles possess work/area factors of at least 3 lbf/ft.

6. The method of claim 2 wherein the bubbles possess work/area factors of at least 4 lbf/ft.

7. The method of claim 1 wherein the waste comprises aerobic, anoxic and anaerobic waste-digestive microorganisms and the quantity of introduced air and agitation are controlled so as to produce in the waste aerobic, anoxic and anaerobic zones.

8. The method of claim 7 wherein the anoxic zone includes a population of denitrifying microorganisms.

9. The method of claim 8 wherein the aerobic zone includes a population of nitrifying microorganisms.

10. The method of claim 1 further comprising the step of controlling the quantity of introduced air and effecting controlled agitation of the waste so as to maintain at least one biological indicator at a predetermined level.

11. The method of claim 10 wherein the indicator comprises at least one of ammonia level;

soluble nitrate level;

soluble nitrite level; and

oxidation-reduction potential.

12. The method of claim 1 wherein the controlled agitation does not exceed a mean velocity gradient of 100 sec^-1.

13. The method of claim 1 wherein the bubbles have an average diameter, and agitation is controlled by adjusting the average diameter.

14. The method of claim 1 wherein the bubbles have an average diameter, and the quantity of introduced air is controlled by adjusting the average diameter.

15. Apparatus of treating liquid-borne waste containing at least two different types of waste-digestive microorganism, the different types of microorganism requiring mutually incompatible chemical environments and comprising an aerobic and a non-aerobic species, the apparatus comprising:

a. a treatment vessel having a bottom;

b. means for introducing a supply of micronized air bubbles into the bottom of the waste-containing treatment vessel, the continuous supply of air bubbles corresponding to a quantity of introduced air thereby creating in the bottom region an aerobic zone compatible with and containing the aerobic species;

c. means for imparting a degree of agitation of the waste; and

d. control means, coupled to the bubble-introduction means, for controlling (i) the quantity of introduced air and (ii) the degree of agitation to produce in the waste at least one distinct non-aerobic zone vertically adjacent to the aerobic zone, the non-aerobic zone having a chemical environment compatible with and containing the non-aerobic species.

16. The apparatus of claim 15 wherein the means for introducing a supply of micronized air bubbles into the bottom of the waste-containing treatment vessel comprises:

a. microporous element having an average pore size;

b. means for exposing a surface of the microporous element to gas at a predetermined pressure; and

c. means for moving a fluid and the microporous element relative to one another with sufficient motive force to achieve a predetermined fluid velocity in excess of 10 ft/sec,

wherein the average pore size of the microporous element is less than 1 micron.

17. The apparatus of claim 15 further comprising means for sensing at least one biological indicator in the vessel and generating a signal indicative thereof, the control means being configured to receive the signal.

18. The apparatus of claim 17 wherein the controller responds to the signal by controlling the quantity of introduced air and effecting controlled agitation of the waste so as to maintain the at least one biological indicator at a predetermined level.

19. The apparatus of claim 17 wherein the sensing means senses at least one of ammonia level;

soluble nitrate level;

soluble nitrite level; and

oxidation-reduction potential.

20. The apparatus of claim 15 wherein agitation is supplied by the bubbles, the agitation means being the bubble-introduction means.

21. The apparatus of claim 20 wherein the bubbles have an average diameter, and agitation is controlled by adjusting the average diameter.

22. The apparatus of claim 15 wherein the agitation means comprises mechanical means for imparting turbulence.

23. The apparatus of claim 15 wherein the degree of agitation does not exceed a mean velocity gradient of 100 sec^-1.

24. The apparatus of claim 15 wherein the bubble-introduction means produces bubbles having an average diameter controllable by the control means, which controls the quantity of introduced air by adjusting the average diameter.