Aquaponic nutrient generation module

1. An aquaponic system comprising:

a. a fish tank containing an aquatic species;

b. a floating media bioclarifier including (i) an influent inlet configured to direct influent through a media bed, (ii) a sludge concentration space beneath the media bed, and (iii) an effluent outlet positioned to receive fluid treated and filtered by the media bed;

c. wherein the bioclarifier influent inlet receives influent from the fish tank and the effluent outlet directs effluent to a return loop ultimately terminating into the fish tank;

d. a mineralization tank receiving sludge having a first solids concentration from the bioclarifier and returning to the bioclarifier a fluid having a second solids concentration less than the first solids concentration; and

e. a hydroponic system configured to selectively receive effluent from the bioclarifier.

2. The aquaponic system of claim 1 , wherein the hydroponic system is incapable of directing fluid to the fish tank.

3. The aquaponic system of claim 1 , wherein the first solids concentration is over 0.5 percent and the second solids concentration is less than 0.5 percent.

4. The aquaponic system of claim 3 , wherein the first solids concentration is between about 1 percent and about 4 percent.

5. The aquaponic system of claim 1 , wherein the fluid having a second solids concentration is returned to the bioclarifier upstream of the media bed.

6. The aquaponic system of claim 1 , wherein no pump is present (1) in a line conveying sludge having the first solids concentration, or (2) in a line conveying the fluid having the second solids concentration.

7. The aquaponic system of claim 1 , wherein a flow of sludge received by the mineralization tank is less than 0.01 percent of a flow of bioclarifier effluent back to the fish tank.

8. The aquaponic system of claim 1 , further comprising a second influent inlet configured to receive influent from the fish tank which has bypassed the bioclarifier.

9. The aquaponic system of claim 8 , wherein a flow rate into the second influent inlet of the mineralization tank is between about 1% and about 5% of a flow rate out of the effluent outlet of the bioclarifier.

10. The aquaponic system of claim 1 , wherein a sludge input line enters the mineralization tank from a point above the water level.

11. An aquaculture system comprising:

a. a fish tank containing an aquatic species;

b. a floating media bioclarifier including (i) an influent inlet configured to direct influent through a media bed, (ii) a sludge concentration space beneath the media bed, and (iii) an effluent outlet downstream of the media bed;

c. wherein the bioclarifier influent inlet receives influent from the fish tank and the effluent outlet directs effluent back to the fish tank;

d. a mineralization tank including (i) a first influent inlet for receiving sludge having a first solids concentration from the bioclarifier, (ii) an effluent outlet for returning to the bioclarifier a fluid having a second solids concentration less than the first solids concentration, and (iii) a second influent inlet configured to receive influent from the fish tank which has bypassed the bioclarifier; and

e. a hydroponic system configured to receive effluent from the bioclarifier.

12. An aquaculture system comprising:

a. a growth tank containing an aquatic species;

b. a floating media bioclarifier including (i) an influent inlet configured to direct influent through a media bed, (ii) a sludge concentration space beneath the media bed, and (iii) an effluent outlet downstream of the media bed;

c. wherein the bioclarifier influent inlet receives influent from the growth tank and the effluent outlet directs effluent back to the growth tank; and

d. a mineralization tank including (i) a first inlet receiving from the bioclarifier sludge having a first solids concentration, (ii) an outlet returning to the bioclarifier a fluid having a second solids concentration less than the first solids concentration, and (iii) a second inlet receiving an inflow from the growth tank, wherein the inflow has bypassed the bioclarifier.

13. An aquaculture system comprising:

a. a growth tank containing an aquatic species;

b. a floating media bioclarifier including (i) an influent inlet configured to direct influent through a media bed, (ii) a sludge concentration space beneath the media bed, and (iii) an effluent outlet downstream of the media bed;

c. wherein the bioclarifier influent inlet receives influent from the growth tank and the effluent outlet directs effluent back to the growth tank; and

d. a mineralization tank including (i) a first inlet receiving from the bioclarifier sludge having a first solids concentration, and (ii) an outlet returning to the bioclarifier a fluid having a second solids concentration less than the first solids concentration.

14. The aquaculture system of claim 13 , wherein the mineralization tank includes a second inlet receiving an inflow from the growth tank, wherein the inflow has bypassed the bioclarifier.

15. The aquaculture system of claim 14 , wherein a flow rate into the second influent inlet of the mineralization tank is less than 10% of a flow rate out of the effluent outlet of the bioclarifier.

16. The aquaculture system of claim 15 , wherein the flow rate into the second influent inlet of the mineralization tank is between about 1% and about 5% of the flow rate out of the effluent outlet of the bioclarifier.

17. The aquaculture system of claim 13 , wherein the mineralization tank further comprises an operating water level and an airlift aerator, the airlift aerator including (i) a tubular body; (ii) an airlift inlet within a lower quarter of the operating water level; and (iii) at least one return path extending from above or within an upper half of the operating water level downward to the lower half of the operating water level.

18. The aquaculture system of claim 17 , wherein the return path is formed by at least one return line connected to the tubular body in an upper quarter of the operating water level and extending downward to have an outlet positioned within the lower third of the operating water level.

19. The aquaculture system of claim 17 , wherein the return path is formed by an outer return flow tube formed concentrically around the airlift tubular body.

20. The aquaculture system of claim 17 , further comprising a sludge input line extending into the mineralization tank, the sludge input line having an outlet in the lower quarter of the operating water level.

21. The aquaculture system of claim 20 , wherein the sludge input line enters the mineralization tank from a point above the water level.

22. The aquaculture system of claim 13 , wherein the mineralization tank includes a gas injection system configured to inject gas into sludge in the mineralization tank during an aerating time period and not inject gas into the sludge during a non-aerating time period, wherein the aerating time period is sufficient to prevent stratification of the sludge.

23. The aquaculture system of claim 22 , wherein the non-aerating time period is at least five times longer than the aerating time period.

24. The aquaculture system of claim 13 , wherein the mineralization tank includes a gas injection system configured (i) to inject gas into the mineralization tank during a first time period to create aerobic digestion conditions and (ii) to not inject gas into the mineralization tank during a second time period to create anaerobic digestion conditions.

25. The aquaculture system of claim 24 , wherein the mineralization tank is operated under aerobic digestion conditions for longer periods of time than operated under anaerobic digestion conditions.

26. The aquaculture system of claim 24 , wherein the mineralization tank is operated under aerobic digestion conditions for at least one hour and operated under anaerobic digestion conditions for at least one hour.

27. The aquaculture system of claim 13 , wherein at least 25% of biodegradable solids of the sludge in the mineralization tank is converted to inorganic components during a residence time.

28. The aquaculture system of claim 13 , wherein sludge in the mineralization tank predominantly undergoes aerobic digestion.

29. The aquaculture system of claim 13 , wherein sludge entering the mineralization tank has an average residence time of at least 5 days.

30. The aquaculture system of claim 13 , wherein sludge in the mineralization tank predominantly undergoes anaerobic digestion.

31. The aquaculture system of claim 13 , wherein the first inlet and the outlet of the mineralization tank communicate with the bioclarifier through a common conduit.