IP Library Granted Patent US 8,864,868
Granted Patent B2
US 8,864,868 · App. 14/084,663 · Granted Oct 21, 2014

Organic containing sludge to fertilizer alkaline conversion process

Inventor: Jeffrey C. Burnham (Beech Island, SC)
Assignee: VitAg Corporation
C05F3/00C02F11/14C05C3/00C05F7/00C05F5/008C05F9/00A45D20/18C02F11/06
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Quick Facts
Patent No.
US 8,864,868
App. No.
14/084,663
Granted
Oct 21, 2014
Kind
B2
Abstract

This invention is directed to systems, devices and methods for treating organic-containing sludges and converting such sludges to high value fertilizers containing both inorganic and organic fertilizer components, which creates an inorganically-augmented bioorganic fertilizer. The invention describes methods to create a thixotropic or paste-like material via the application of mixing energy to the organic sludge followed by an alkaline treatment and a subsequent ammoniation. The invention further describes a method to increase the plant nutrient content in the organic containing product to a level which permits the finished granular fertilizer product to compete in the commercial agricultural fertilizer marketplace. Further, the invention reduces odors associated with said organic-containing sludges.

Claims (38)

1. A method of fertilizer manufacture comprising:

creating a thixotropic paste from a composition containing biosolids;

adding an alkaline agent to the paste to produce a pH of 10 or higher;

exposing the paste to ammonia at a concentration of at least 1,000 ppm

adding an acid to the paste to produce heat and a pH 7.0 or less;

drying the paste to a dryness of 90% or more of solids.

2. The method of claim 1 , wherein the biosolids are selected from the group consisting of municipal biosolids and sludges, manures and animal residuals, lagoon sludges, organic-containing sludges produced from food fermentation, sludge waste products, pharmaceutical fermentation waste industrial fermentation products, and mixture and combinations thereof.

3. The method of claim 1 , further comprising adding as an oxidizing agent hypochlorite, sodium hypochlorite, calcium hypochlorite, iron oxide, metal oxide, calcium ferrate, potassium ferrate, sodium ferrate, oxygen, hydrogen peroxide, peroxide, ozone, chlorine dioxide, or a combination thereof.

4. The method of claim 1 , wherein the alkaline agent is selected from the group consisting of calcium oxide, calcium hydroxide, potassium hydroxide, sodium hydroxide, alkaline by products, cement kiln dust, lime kiln dust, Class C fly ash, Class F fly ash, lime-injected fly ash, high-alkaline materials, and combinations thereof.

5. The method of claim 1 , wherein, after addition of the alkaline agent, the mixture is pH 11 or higher.

6. The method of claim 1 , wherein the ammonia is aqueous or anhydrous ammonia.

7. The method of claim 1 , wherein the concentration of ammonia is at least 5,000 ppm.

8. The method of claim 1 , wherein the concentration of ammonia is at least 10,000 ppm.

9. The method of claim 1 , wherein the concentration of ammonia is at least 20,000 ppm.

10. The method of claim 1 , wherein the exposure is for at least 30 seconds.

11. The method of claim 1 , wherein the exposure is for at least 2 minutes.

12. The method of claim 1 , wherein the exposure is for at least 5 minutes.

13. The method of claim 1 , wherein the concentration of ammonia provides a dry weight nitrogen concentration of 6%.

14. The method of claim 1 , wherein the concentration of ammonia provides a dry weight nitrogen concentration of 10%.

15. The method of claim 1 , wherein the concentration of ammonia provides a dry weight nitrogen concentration of 14%.

16. The method of claim 1 , wherein, after addition of the alkaline agent, the mixture is pH 11 or higher.

17. The method of claim 1 , wherein the acid is phosphoric or sulfuric acid.

18. The method of claim 1 , wherein the concentrated acid is selected from the group consisting of phosphoric acid, sulfuric acid, sulfamic acid, hydrochloric acid, nitric acid and combinations thereof.

19. The method of claim 1 , wherein, after treating with the acid, the paste is pH 7.0 or less.

20. The method of claim 1 , further comprising blending a plant nutrient with the thixotropic paste to increase nitrogen, phosphorus and iron levels.

21. The method of claim 20 , wherein the plant nutrient content is at least 8% nitrogen by dry weight.

22. The method of claim 20 , wherein the plant nutrient content is at least 12% by dry weight.

23. The method of claim 20 , wherein the plant nutrient content is at least 15% by dry weight.

24. The method of claim 1 , wherein odor associated with the paste is reduced.

25. The method of claim 1 , wherein the thixotropic paste is treated with an oxidizing agent such that odorants emission is reduced simultaneously with increasing plant nutrient concentration.

26. The method of claim 1 , wherein the extruded paste is formed into pellets or granules.

27. The method of claim 26 , wherein the pellets or granules are coated.

28. The method of claim 1 , further comprising storing the dried paste in a dry environment.

29. The method of claim 1 , further comprising applying the dried paste to plants as a fertilizer.

30. The method of claim 1 , further comprising applying an antimicrobial stress during any step.

31. The method of claim 30 , wherein the microbial stress is selected from the group consisting of a pH greater than pH 10, a pH greater than pH 11.0; free ammonia concentration in the paste at greater than 1,000 ppm, free ammonia concentration in the paste at greater than 10,000 ppm; free ammonia concentration in the paste at greater than 15,000 ppm; heat at greater than 80° C.; greater than 100° C., heat at greater than 121° C. and combinations thereof.

32. The method of claim 1 , further comprising adding a fertilizer to the dried pellets or granules to provide nutrient enhancement.

33. The method of claim 32 , wherein the fertilizer is selected from the group consisting of dry fertilizers, liquid fertilizers, ammonium sulfate, ammonium nitrate, mono-ammonium phosphate, di-ammonium phosphate, urea, urea ammonium nitrate (“UAN”), liquid urea, liquid N-P-K fertilizers, 16-4-8, 10-8-8, 6-14-6, and combinations thereof.

Assignments (8)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 13, 2023
From: ANUVIA PLANT CITY LLC; ANUVIA PLANT NUTRIENTS HOLDINGS INC.; ANUVIA PLANT NUTRIENTS IP HOLDINGS LLC; ANUVIA PLANT NUTRIENTS CORPORATION
To: PROFILE PRODUCTS LLC
Reel/Frame 064896/0805 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 2, 2023
From: ANUVIA PLANT NUTRIENTS HOLDINGS INC.; ANUVIA PLANT NUTRIENTS IP HOLDINGS LLC
To: GENERATE LENDING, LLC
Reel/Frame 062926/0436 →
RELEASE OF SECURITY INTEREST Recorded Feb 11, 2021
From: PONTIFAX AGTECH INVESTMENTS: ANUVIA SERIES C BRIDGE, LLC
To: ANUVIA PLANT NUTRIENTS HOLDINGS, INC.; ANUVIA PLANT NUTRIENTS CORPORATION; ANUVIA PLANT NUTRIENTS IP HOLDINGS LLC; ANUVIA PLANT CITY LLC
Reel/Frame 055239/0028 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 30, 2020
From: ANUVIA PLANT NUTRIENTS CORPORATION
To: ANUVIA PLANT NUTRIENTS IP HOLDINGS LLC
Reel/Frame 054777/0465 →
SECURITY INTEREST Recorded Sep 15, 2020
From: ANUVIA PLANT NUTRIENTS HOLDINGS INC.; ANUVIA PLANT CITY LLC; ANUVIA PLANT NUTRIENTS CORPORATION
To: PONTIFAX AGTECH INVESTMENTS: ANUVIA SERIES C BRIDGE, LLC
Reel/Frame 053770/0885 →
RELEASE OF SECURITY INTEREST Recorded Aug 17, 2018
From: TCPC SBIC, LP
To: ANUVIA PLANT NUTRIENTS CORPORATION; VITAG HOLDINGS LLC
Reel/Frame 046859/0828 →
CHANGE OF NAME Recorded Jul 28, 2015
From: VITAG CORPORATION
To: ANUVIA PLANT NUTRIENTS CORPORATION
Reel/Frame 036192/0211 →
SECURITY INTEREST Recorded Jul 11, 2014
From: VITAG CORPORATION; VITAG HOLDINGS LLC
To: TCPC SBIC, LP
Reel/Frame 033303/0914 →
Continuity (6)
Continuation 13472843 · May 16, 2012
Continuation 13103637 · May 9, 2011
Continuation 12705813 · Feb 15, 2010
Continuation 11521604 · Sep 15, 2006
Provisional Application 60716964 · Sep 15, 2005
Related Publication 20140150507A1 · Jun 5, 2014