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A system and method are provided for removal of undesirable substances from a body of liquid. The system can include an aeration structure having a continuously inclined surface configured to provide an interaction of air bubbles against substantially an entire length of the continuously inclined su

A system and method are provided for removal of undesirable substances from a body of liquid. The system can include an aeration structure having a continuously inclined surface configured to provide an interaction of air bubbles against substantially an entire length of the continuously inclined surface while the air bubbles are moving toward a top of the body of liquid. The continuously inclined surface can be substantially submerged in the body of liquid. A bio-film of diverse bacteria colonies is disposed on the continuously inclined surface, and a high surface area-to-volume structure is located in proximity to the aeration structure, upon which a bio-film of bacteria colonies can be formed. An aeration system is coupled to an air supply system which releases the air bubbles toward a bottom of the continuously inclined surface, such that the air bubbles move along the continuously inclined surface as they rise so as to (i) create a variety of aerobic-anaerobic conditions at the bio-film and (ii) engage the air bubbles in a continuous mixing of a micro climate for the bio-film in response to an orientation of the continuously inclined surface and (iii) provide airlift circulation of water from bottom to top of the aeration structure.

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1. A system for removal of undesirable substances from a body of liquid, comprising: an aeration structure constructed of a pipe having a continuously inclined surface configured to provide an interaction of air bubbles against substantially an entire length of the continuously inclined surface whil

1. A system for removal of undesirable substances from a body of liquid, comprising: an aeration structure constructed of a pipe having a continuously inclined surface configured to provide an interaction of air bubbles against substantially an entire length of the continuously inclined surface while moving toward a top of the body of liquid, the continuously inclined surface being substantially submerged in the body of liquid;a bio-film of bacteria disposed on the continuously inclined surface;a high surface area-to-volume structure located within the pipe upon which a bio-film of bacteria can be formed;an aeration system, couplable to an air supply system, configured to release the air bubbles toward a bottom of the continuously inclined surface, such that the air bubbles move along the continuously inclined surface and the high surface-to-volume structure as the air bubbles rise so as to (i) create a variety of aerobic-anaerobic conditions for the bio-film and (ii) create a bottom-to-top circulation pattern to provide selective air mixing to support a micro climate for the bio-film on exposed surfaces. 2. A system as in claim 1, wherein a second aeration structure is formed that is nested within the aeration structure and the high surface area-to-volume structure is located between the first aeration structure and the second aeration structure. 3. A system as in claim 1, wherein the high surface area-to-volume structure is held in position within the pipe by a retainer selected from the group consisting of: netting, a wire guide, a retainer at a bottom of the aeration structure, a plurality of flanges on the bottom of the aeration structure and a grill. 4. A system as in claim 1, wherein the high surface area-to-volume structure further comprises a high surface area-to-weight packing media. 5. A system as in claim 1, wherein aerobic bacteria grow at an exposed surface of the bio-film of the high surface area-to-volume structure and anaerobic bacteria are promoted in an area close to a substrate surface of the high surface area-to-volume structure. 6. A system as in claim 1, wherein movement of the bubbles circulates at least a portion of the body of liquid near the continuously inclined surface and through the high surface area-to-volume structure. 7. A system as in claim 1, wherein a bio-film on a surface of an outer wall of the aeration structure can have an aerobic environment, the bio-film on the high surface area-to-volume structure can have a moderately aerobic environment, and a bio-film on an exterior surface of an inner wall opposing the outer wall of the aeration structure is a substantially anoxic environment. 8. A system as in claim 1, wherein the aeration structure has a rough surface to promote bio-film growth. 9. A system as in claim 1, wherein the aeration structure has a rough surface formed by sand granules to promote bio-film growth. 10. A system as in claim 1, further comprising a second aeration structure with an inlet of the second aeration structure horizontally connected to an outlet of the first aeration structure. 11. A system as in claim 1, further comprising a second aeration structure with an inlet of the second aeration structure vertically connected to an outlet of the first aeration structure. 12. A system for removal of undesirable substances from a body of liquid, comprising: an aeration structure constructed of a pipe having a continuously inclined surface configured to provide a continuous interaction of air bubbles against substantially an entire length of the continuously inclined surface while moving toward a top of the body of liquid, the continuously inclined surface being substantially submerged in the body of liquid;a bio-film of bacteria disposed on the continuously inclined surface;a high surface area-to-volume structure located within the pipe upon which a bio-film of bacteria can be formed;a heater located in proximity to the aeration structure configured to provide a warmer environment for the bio-film; andan aeration system, couplable to an air supply system, configured to release the air bubbles toward a bottom of the continuously inclined surface, such that the air bubbles move along the continuously inclined surface as they rise so as to (i) create a variety of aerobic conditions at the bio-film and (ii) engage the air bubbles in a continuous mixing of a micro climate for the bio-film in response to an orientation of the continuously inclined surface (iii) circulate water bottom to top using air bubble lift. 13. A system as in claim 12, wherein the heater is a water heater located at a bottom of the aeration structure, the water heater being configured to heat water that will travel up through the aeration structure and promote bio-film growth. 14. A system as in claim 12, wherein the heater is located on an interior wall surface of the aeration structure. 15. A system as in claim 12, wherein the heater is a resistive electrical heater located on an interior wall surface of the aeration structure and configured to heat the aeration structure and a portion of the liquid. 16. A system as in claim 12, wherein the heater is a resistive electrical heater that is embedded within the aeration structure and configured to heat the aeration structure. 17. A system as in claim 12, further comprising an air source heater included in the air supply system to provide heated air bubbles that promote bio-film growth. 18. A system as in claim 12, further comprising an air source heater included in the air supply system to provide heated air bubbles that pass through a passage within the aeration structure to promote bio-film growth. 19. A system as in claim 12, further comprising a solar collection structure that is attached in proximity to the aeration structure to provide power for aeration or heat. 20. A system as in claim 12, wherein the air supply system comprises a windmill that provides power to the air supply system to inject compressed air at the bottom of the continuously inclined surface. 21. A system for removal of undesirable substances from a body of liquid, comprising: a plurality of aeration structures constructed of a pipe having a continuously inclined surface configured to provide an interaction of air bubbles against a length of the continuously inclined surface while moving toward a top of the body of liquid, the continuously inclined surface being substantially submerged in the body of liquid, wherein substantially the entire continuously inclined surface is at an incline;a bio-film of bacteria colonies disposed on the continuously inclined surface used to breakdown organic material;a high surface area-to-volume structure located within the pipe upon which a bio-film of bacteria can be formed;a circuit channel formed in the body of liquid within which the plurality of aeration structures are located; andan aeration system, couplable to an air supply system, configured to release the air bubbles on demand toward a bottom side of the continuously inclined surface, such that the air bubbles move along the continuously inclined surface and the high surface-to-volume structure as they rise so as to (i) create a variety of aerobic-anaerobic conditions for the bio-film and (ii) create a bottom-to-top circulation pattern to provide nutrient and air mixing to support a micro climate for the bio-film on exposed surfaces. 22. A system as in claim 21, further comprising a first portion of the circuit channel having an aeration system and a second portion of the circuit channel having no aeration system. 23. A system as in claim 22, wherein the portion of the circuit channel having an aeration system further comprises a zone where aerobic bacteria colonize the bio-film to nitrify ammonia nitrogen. 24. A system as in claim 22, wherein the portion of the circuit channel without an aeration system further comprises a zone where anoxic bacteria colonize the bio-film to denitrify nitrites and nitrates from the liquid. 25. A system as in claim 21, wherein the aeration system is configured to provide aeration for a first timed period and then the aeration system is turned off for a second timed period. 26. A system as in claim 25, wherein turning on the aeration system enables the bio-film to aerobically uptake phosphorous compounds from liquid processed during the aerobic period that are discharged via a primary discharge conduit. 27. A system as in claim 26, wherein the aeration system in the body of liquid is turned off for a pre-set time period to allow the phosphorous compounds disgorged from the bio-film to be diverted via a secondary discharge conduit and to be held in a separate retaining body of liquid. 28. A system as in claim 21, further comprising a first portion of the circuit channel being highly aerated, a second portion of the circuit channel having moderate aeration and a third portion of the circuit channel being non-aerated. 29. A method for removing undesirable substances from a body of liquid, comprising: directing a portion of the body of liquid to flow through a circuit channel formed using at least one guidance wall in the body of liquid;submerging a plurality of aeration structures constructed of a pipe in the circuit channel, the pipe having a continuously inclined surface in the body of liquid and substantially the entire continuously inclined surface of each aeration structure is at an incline;enabling a variety of bio-film bacterial colonies to be disposed on the continuously inclined surfaces and high surface-to-volume structure surfaces located within the pipe;releasing air at a defined point on the continuously inclined surface using an aeration system, couplable to an air supply system, such that air bubbles are formed and move along the continuously inclined surface as they rise so as to (i) create a variety of aerobic and anaerobic conditions for the bio-film and (ii) create a bottom-to-top circulation pattern to provide nutrient and air mixing to support a micro climate for the bio-film on exposed surfaces. 30. A method as in claim 29, further comprising placing an aeration system in a first portion of the circuit channel and providing a second portion of the circuit channel having no aeration system. 31. A method as in claim 30, wherein a defined point on the continuously inclined surface further comprises the bottom of the continuously inclined surface, a middle point of the continuously included surface, or a top point of the continuously included surface. 32. A method as in claim 29, further comprising activating the aeration system to provide aeration for a timed period and deactivating the aeration for a timed period. 33. A method as in claim 29, further comprising: activating the aeration system to enable aerobic bio-film to capture phosphorous compounds from waste liquid and discharging fluid when aeration is active; anddisabling the aeration system so as to disgorge phosphorous compounds from the bio-film while diverting fluid from the body of liquid to be held in a separate retaining pond.