Hydrothermal carbonization of sewage wastes

Patent metadata

Field	Value
Publication number	US-9475698-B2
Application number	US-201314406955-A
Country	US
Kind code	B2
Filing date	Mar 8, 2013
Priority date	Jun 15, 2012
Publication date	Oct 25, 2016
Grant date	Oct 25, 2016

Abstract

The present disclosure provides methods for hydrothermally treating sewage wastes to preferably obtain valuable products, including fatty acids, carbon-neutral combustible hydrochar fuels, heavy metal salts for recycling into industrially important metals, and phosphoric acid and derivatives thereof. Fatty acids can be chemically transformed into useful products such as soaps, cosmetics and liquid transportation fuels such as biodiesel and conventional gasoline, diesel and aviation fuels; hydrochars created in the process can be combusted and the energy created used to generate electricity; heavy metal salts can be chemically reduced to form industrially important metals for use as catalysts; and phosphoric acid and its derivatives have very important roles as fertilizers in agriculture.

First claim

What is claimed is:

1. A method of obtaining a phosphate from a sewage material, the method comprising:
subjecting a wet sewage material to a hydrothermal carbonization process to produce a hydrochar and an aqueous product stream;
isolating the hydrochar from the aqueous product stream;
treating at least a portion of the isolated hydrochar with an aqueous acid under conditions effective to provide an aqueous phosphate material; and
isolating the acid-treated hydrochar from the aqueous phosphate material.

2. The method of claim 1 wherein the aqueous phosphate material is suitable for use as a fertilizer, or as a feedstock for anaerobic digestion without further processing.

3. The method of claim 1 wherein the aqueous phosphate material includes heavy metals, and the method further comprises removing at least a portion of the heavy metals from the aqueous phosphate material.

4. The method of claim 1 further comprising removing at least a portion of the water from the aqueous phosphate material to provide a dewatered phosphate material.

5. The method of claim 4 wherein removing at least a portion of the water comprises a process selected from the group consisting of evaporation, distillation, membrane removal, and combinations thereof.

6. The method of claim 5 wherein the membrane removal process comprises crossflow filtration or dialysis separation.

7. The method of claim 4 wherein the dewatered phosphate material is suitable for use without further processing as a fertilizer.

8. The method of claim 1 wherein the wet sewage material comprises one or more materials selected from the group consisting of human wastes, dairy cattle manures, beef cattle manures, swine manures, poultry manures, and horse manures.

9. The method of claim 1 wherein water is added to the wet sewage material to adjust the solids content.

10. The method of claim 1 wherein the wet sewage material has a solids content of 0.25% to 30% by weight.

11. The method of claim 1 wherein the wet sewage material has a cellulose content of less than 50% by weight.

12. The method of claim 1 wherein at least one multivalent cation is added to the wet sewage material.

13. The method of claim 12 wherein the at least one multivalent cation forms a phosphate salt having a solubility product constant (Ksp) of less than 10 −5 .

14. The method of claim 12 wherein the at least one multivalent cation forms a phosphate salt having a solubility product constant (Ksp) of less than 10 −8 .

15. The method of claim 12 wherein the at least one multivalent cation forms a phosphate salt having a solubility product constant (Ksp) of less than 10 −5 .

16. The method of claim 12 wherein the at least one multivalent cation forms a phosphate salt having a solubility product constant (Ksp) of less than 10 −35 .

17. The method of claim 12 wherein 0.1% to 10% by weight of the at least one multivalent cation is added to the wet sewage material, based on the total dry solids of the sewage material.

18. The method of claim 12 wherein the at least one multivalent cation is selected from the group consisting of Al, Ca, Mg, Fe, Zn, and combinations thereof.

19. The method of claim 1 wherein the temperature of the hydrothermal carbonization process is 185° C. to 225° C.

20. The method of claim 1 wherein the time of the hydrothermal carbonization process is 0.25 hours to 2 hours.

21. The method of claim 1 wherein the pressure of the hydrothermal carbonization process is 10 to 26 atmospheres.

22. The method of claim 1 wherein the initial pH of the wet sewage material in the hydrothermal carbonization process is 4 to 8.

23. The method of claim 1 wherein isolating the hydrochar from the aqueous product stream comprises filtration, centrifugation, or a combination thereof.

24. The method of claim 1 wherein the aqueous product stream is suitable for use as a fertilizer or an anaerobic digestion substrate without further processing.

25. The method of claim 1 wherein isolating the acid-treated hydrochar and/or acid and organic solvent-treated hydrochar from the aqueous phosphate material comprises filtration, centrifugation, or a combination thereof.

26. The method of claim 1 wherein untreated and/or treated hydrochar is suitable for use directly as carbon-neutral energy products.

27. The method of claim 1 wherein the wet sewage material is untreated.

28. The method of claim 1 further comprising combusting at least a portion of the isolated hydrochar and/or the isolated organic solvent-treated hydrochar to form an ash.

29. The method of claim 28 further comprising treating at least a portion of the ash with an aqueous acid under conditions effective to provide an aqueous phosphate material and/or heavy metals.

30. A method of obtaining a phosphate from a sewage material, the method comprising:
subjecting a wet sewage material to a hydrothermal carbonization process at a temperature of 185° C. to 225° C. and a pressure of 10 to 26 atmospheres to produce a hydrochar and an aqueous product stream;
isolating the hydrochar from the aqueous product stream using filtration and/or centrifugation;
treating at least a portion of the isolated hydrochar with an aqueous acid under conditions effective to provide an aqueous phosphate material; and
isolating the acid-treated hydrochar from the aqueous phosphate material using filtration and/or centrifugation.

31. The method of claim 30 further comprising removing at least a portion of the water from the aqueous phosphate material to provide a dewatered phosphate material.

32. The method of claim 31 wherein removing at least a portion of the water comprises a process selected from the group consisting of evaporation, distillation, membrane removal, and combinations thereof.

33. The method of claim 32 wherein the membrane removal process comprises crossflow filtration or dialysis separation.

Assignees

• Univ Minnesota

Inventors

• Heilmann Steven M
• Schendel Frederick J
• Von Keitz Marc Gregor
• Valentas Kenneth J
• Mikula Anthony L
• Wood Brandon Michael

Classifications

• C02F1/44

  by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title

• C02F9/00

  Multistage treatment of water, waste water or sewage · CPC title

• C01B25/375 Primary

  of iron · CPC title

• C10L9/08

  by heat treatments, e.g. calcining · CPC title

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title