Nutrient recovery process

• US 20080053913A1
• Filed: 09/06/2006
• Published: 03/06/2008
• Est. Priority Date: 09/06/2006
• Status: Abandoned Application

• Current Assignee: Alexander G. Fassbender
• Original Assignee: Alexander G. Fassbender
• Inventors: Fassbender, Alexander G.
• Application Number:
  US11/517,217
• Publication Number:
  US 20080053913A1
• Time in Patent Office: Days
• US Class Current: 210/702
• 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 1/5236 using inorganic agents
• CPC Class Codes: C02F 1/56 Macromolecular compounds
• CPC Class Codes: C02F 1/74 with air aeration of stretches of water C02F7/00
• CPC Class Codes: C02F 2101/105 Phosphorus compounds
• CPC Class Codes: C02F 2101/16 Nitrogen compounds, e.g. ammonia
• CPC Class Codes: C02F 2201/006 Cartridges
• CPC Class Codes: C02F 2301/063 Underpressure, vacuum
• CPC Class Codes: C02F 3/28 Anaerobic digestion processes
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage

Abstract

Embodiments include a method and apparatus for cost-effective and efficient nutrient recovery from a waste stream. The nutrients recovered may include ammonia, phosphorous, and/or potassium. The ammonia and phosphorous recovery may be simultaneously accomplished. In some embodiments, ammonia is recovered along with other nutrients using lime or lime-based products.

Claims

1. A method of recovering ammonia and precipitating phosphorous from a waste stream, comprising:

separating an anaerobically digested waste stream into a solids-rich stream and an solids-depleted stream;

reacting the solids-depleted stream with lime or a lime-based solution to form a first mixture;

introducing compressed gas into the first mixture to form an aerated first mixture;

passing the aerated first mixture through a reaction zone;

passing the aerated first mixture stream through a flocculation zone, where a flocculation agent is added to the aerated first mixture to form a second mixture;

passing the second mixture stream through a settling zone, thereby removing precipitated settled solids from the second mixture stream and removing an ammonia-laden gas and a softened solids-depleted stream from the second mixture stream via sparged compressed gas;

scrubbing the ammonia-laden gas using an acidic solution to remove ammonia therefrom; and

passing at least a portion of the softened solids-depleted stream through at least one ammonia absorption column to remove ammonia therefrom,

wherein introducing the compressed gas into the first mixture removes ammonia and enhances phosphorous precipitation.

2. The method of claim 1, wherein the lime or lime-based solution comprises calcium hydroxide, calcium oxide, or a combination thereof.

3. The method of claim 1, wherein the lime or lime-based solution comprises finely-divided crystalline calcium carbonate [CaCO₃] particles, milk of lime [Ca(OH)₂], lime-water, or a combination thereof.

4. The method of claim 1, wherein the reaction zone, flocculation zone, and settling zone are disposed in an enclosed vessel maintained under a vacuum.

5. The method of claim 1, wherein scrubbing the ammonia-laden gas using the acidic solution is accomplished using an acid scrubber.

6. The method of claim 5, further comprising:

recovering as ammonium salt product a first portion of scrubbed, ammonia-laden gas from the acid scrubber when the first portion becomes saturated with ammonium salt.

7. The method of claim 6, further comprising scrubbing a second portion of the ammonia-laden gas exiting the acid scrubber using a neutral solution;

and

recycling the second portion of the ammonia-laden gas into the reaction zone.

8. The method of claim 7, further comprising compressing the second portion of the ammonia-laden gas prior to its recycling into the reaction zone.

9. The method of claim 8, further comprising heating the second portion of the ammonia-laden gas prior to its recycling into the reaction zone.

10. The method of claim 1, further comprising passing the at least a portion of the softened solids-depleted stream through one or more filters before passing the at least a portion of the softened solids-depleted stream through the at least one ammonia absorption column.

11. The method of claim 10, wherein the one or more filters comprise one or more multi-media filters and one or more cartridge filters.

12. The method of claim 10, wherein:

a first portion of the softened solids-depleted stream passing from the one or more filters is passed to the at least one ammonia absorption column; and

a second portion of the softened solids-depleted stream passing from the one or more filters is recycled to the reaction zone.

13. The method of claim 10, further comprising passing the at least the portion of the softened solids-depleted stream through one or more cation exchange softeners after passing the at least a portion of the softened solids-depleted stream through the one or more filters and before passing the at least a portion of the softened solids-depleted stream through the at least one ammonia absorption column.

14. The method of claim 1, further comprising:

passing a first portion of the at least a portion of the softened solids-depleted stream exiting from the at least one ammonia absorption column into ammonium salt product recovery, the first portion comprising ammonia vapor; and

neutralizing a second portion of the at least a portion of the softened solids-depleted stream exiting from the at least one ammonia absorption column to recover a treated product stream.

15. The method of claim 14, further comprising:

passing the second portion of the at least a portion of the softened solids-depleted stream through one or more ion exchange columns prior to neutralizing the second portion to remove remaining ammonia and potassium therefrom; and

sending the removed ammonia to ammonium salt product recovery.

16. The method of claim 14, wherein the softened solids-depleted stream has a pH of approximately 10.5, and wherein the treated product stream has a pH of from approximately 6 to approximately 8.

17. The method of claim 16, wherein the pH of the solids-depleted stream is approximately 7.

18. The method of claim 1, wherein the compressed gas comprises a plurality of gas bubbles, a first portion of the gas bubbles jetted at a higher velocity than a second portion of the gas bubbles.

19. The method of claim 1, further comprising optimizing a jetting velocity of compressed gas bubbles to induce a desired shear rate of ammonia from the waste stream.

20. An apparatus for removing ammonia and phosphorous from a waste stream, comprising:

a reacting and settling vessel comprising;

at least one reaction chamber for reacting a lime or lime-based product with a solids-depleted stream,

at least one flocculation chamber for adding a flocculating agent to the solids-depleted stream,

at least one settling chamber for settling and precipitating a solids stream from an ammonia-laden gas, and

a capability to recirculate at least a portion of settled solids back to the at least one reaction chamber;

at least one gas compressor for compressing a gas prior to its introduction into the at least one reaction chamber; and

at least one ammonia absorption column for separating ammonia from the compressed gas subsequent to its contact in at least one of the chambers of the reacting and settling vessel, wherein the compressed gas removes ammonia from the solids-depleted stream and enhances phosphorous precipitation.

21. The apparatus of claim 20, further comprising one or more filtering devices located downstream from the reacting and settling vessel and upstream from the at least one ammonia absorption column.

22. The apparatus of claim 21, wherein the one or more filtering devices comprise one or more multi-media filters.

23. The apparatus of claim 22, wherein the one or more filtering devices further comprise one or more cartridge filters.

24. The apparatus of claim 20, further comprising one or more ion exchange softening columns located downstream from the reacting and settling vessel and upstream from the at least one ammonia absorption column.

25. The apparatus of claim 20, further comprising one or more ammonia polishing columns disposed downstream of the at least one ammonia absorption column.

26. The apparatus of claim 20, further comprising one or more scrubbing devices disposed downstream from the reacting and settling vessel for acid scrubbing an ammonia-laden gas removed from the reacting and settling vessel.

27. The apparatus of claim 26, wherein the one or more scrubbing devices comprise one or more acid scrubbers.

28. The apparatus of claim 27, wherein the one or more scrubbing devices further comprise one or more neutral scrubbers.

29. A method for slow softening a waste stream having soluble calcium compounds present therein, wherein at least one alkaline precipitating agent is admixed with the waste stream to be softened in a mixing zone and then the calcium compounds are changed inside a reaction zone through which the waste stream passes after being admixed with the alkaline precipitating agent into insoluble calcium carbonate matter which is subsequently changed in a flocculation zone into settleable flocs by the addition of a flocculating agent containing trivalent metal ions, comprising:

(1) mixing the waste stream, the alkaline precipitating agent, and an agitated liquid, gas, or combination of liquid and gas with finely divided crystalline calcium carbonate in the mixing zone prior to the addition of and in the absence of the flocculation agent to form seeds for the calcium carbonate matter which newly precipitates from the waste stream inside the reaction zone;

(2) presettling and discharging at least a part of the insoluble calcium carbonate matter which has been precipitated inside the reaction zone;

(3) passing the waste stream into a flocculating zone, wherein the waste stream is mixed with the flocculating agent; and

(4) passing the waste stream into a sedimentation zone.

30. The method of claim 29, wherein separated products exiting from the sedimentation zone comprise precipitated solids, a softened waste stream, and ammonia-laden gas.

31. The method of claim 30, further comprising recycling the ammonia-laden gas into the mixing zone to act as the agitated liquid, gas, or combination of liquid and gas in step (1).

32. The method of claim 30, further comprising:

(5) removing ammonia from the softened waste stream using at least one ammonia absorption column.

33. The method of claim 29, wherein at least 5 g/m³ of the finely divided calcium carbonate is added to the mixing zone in step (1).

34. The method of claim 29, wherein the waste stream is wastewater.

35. The method of claim 29, wherein the agitated liquid, gas, or combination of liquid and gas is a compressed gas.

36. The method of claim 35, wherein the compressed gas comprises one or more gas bubbles.

37. The method of claim 29, wherein the mixing zone, flocculation zone, and sedimentation zone are disposed in an enclosed vessel maintained under a vacuum.

38. The method of claim 29, further comprising anaerobically digesting the waste stream prior to step (1).