Food, animal, vegetable and food preparation byproduct treatment apparatus and process

• US 6,464,875 B1
• Filed: 04/21/2000
• Issued: 10/15/2002
• Est. Priority Date: 04/23/1999
• Status: Expired due to Term

• Current Assignee: Pilgrims Pride Corporation (Foster Poultry Farms Incorporated)
• Original Assignee: Gold Kist, Inc.
• Inventors: Woodruff, Steven R.
• Primary Examiner(s): Simmons, David A.
• Assistant Examiner(s): PRINCE JR, FREDDIE GARY
• Application Number:
  US09/556,957
• Time in Patent Office: 907 Days
• Field of Search: 210/603, 210/609, 210/612, 210/613, 210/195.1, 210/252, 210/259, 210/360.1, 210/512.1, 210/513, 210/903, 71/10, 71/14, 71/15, 71/23, 71/25
• US Class Current: 210/603
• CPC Class Codes: C02F 1/586 by removing ammoniacal nitrogen for biological methods C02F3/00
• CPC Class Codes: C02F 2103/22 from the processing of animals, e.g. poultry, fish, or parts thereof
• CPC Class Codes: C02F 3/28 Anaerobic digestion processes
• CPC Class Codes: C05F 17/10 Addition or removal of substances other than water or air to or from the material during the treatment for activating or stimulating the treatment C05F17/20
• CPC Class Codes: C05F 17/40 Treatment of liquids or slurries
• CPC Class Codes: C05F 7/00 Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
• CPC Class Codes: Y02A 40/20 Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02P 20/10 Process efficiency
• CPC Class Codes: Y02P 20/145 the feedstock being materials of biological origin
• CPC Class Codes: Y02W 30/40 Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

A system and method for converting animal, vegetable, and food byproduct materials into useful bio-gas and fertilizer, and/or soil amendment products has an anaerobic digester, a liquid-solids separating unit, an ammonia stripper, an ammonia absorption unit, a solids processing unit, and an equilization tank. The system and method use anaerobic digestion to break down the fats, oils, and greases, proteinaceous, and carbonaceous substances contained in the byproducts. Anaerobic digestion creates bio-gas, mainly methane and carbon dioxide, waste biosolids, which can contain phosphorous, nitrogen and other trace minerals, and a liquid effluent with significant ammonia levels. Ammonia, a useful ingredient for fertilizer formulation, is recovered from the effluent. The solids and the extracted ammonia and/or phosphorous can also be used to make fertilizer and/or soil amendment materials. The bio-gas can be used to fuel various energy recovery devices, such as boilers for steam generation, gas engine generator systems for power generation.

Claims

1. A method of converting animal, vegetable, and food byproducts into useful bio-gas and fertilizer, comprising:

anaerobically digesting or breaking down the byproducts in an anaerobic digester to produce bio-gas containing methane and an effluent;

collecting and storing the bio-gas from the digester into a tank;

transferring the effluent to an ammonia stripper to remove ammonia from the effluent;

transferring the ammonia vapor from the ammonia stripper to an ammonia absorption unit to absorb the ammonia component into an aqueous solution to form an ammonium solution; and

separating the effluent from the ammonia stripper into liquid effluents and solid effluents.

2. A method according to claim 1 further comprising:

conditioning the byproducts with a conditioning agent to enhance anaerobic digestion before introducing the byproducts into the anaerobic digester;

dewatering the solid effluents after separating the liquid effluent to form a slow release fertilizer compound.

3. A method according to claim 1, wherein the ammonia vapor from the ammonia stripper is transferred to an ammonia absorption unit to absorb the ammonia component into an acidic aqueous solution.

4. The method according to claim 1, wherein said animal, vegetable, and food byproducts have a total Kjeldahl nitrogen content of at least about 2700 mg/L.

5. The method according to claim 1, wherein said animal, vegetable, and food byproducts have a fat, oil and grease content of at least about 0.6%.

6. A system for converting animal, vegetable, and food byproducts into useful bio-gas and fertilizer, comprising:

an anaerobic digester that digests or breaks down the byproducts and produces bio-gas containing methane and effluent;

an ammonia stripper that receives the effluent from the anaerobic digester and removes an ammonia component from the effluent as an ammonia vapor;

an ammonia absorption unit that receives the ammonia vapor from the ammonia stripper and absorbs the ammonia component into an aqueous solution to form an ammonium solution; and

a liquid-solids separating unit that receives effluent from the ammonia stripper and separates solids from liquid effluent.

7. A system according to claim 6, further including an equalization tank for conditioning the byproducts before the byproducts are introduced into the anaerobic digester.

8. A system according to claim 6, further including a solids processing unit for dewatering the solids received from the liquid-solids separating unit.

9. A system according to claim 6, wherein the liquid-solids separating unit comprises a centrifuge.

10. A system according to claim 6, wherein the ammonia stripper comprises at least one set of a surge tank and a column feeding into the surge tank, and an air blower for blowing air into the column, wherein the ammonia component in the liquid effluent is transferred into the ammonia vapor by flowing air through the column while the liquid effluent is circulated from the surge tank through the column.

11. A system according to claim 10, wherein the liquid effluent is circulated through the column in a first direction and the air is directed into the column in a second direction, which is opposite to the first direction.

12. A system according to claim 6, wherein the ammonia absorbing unit comprises at least one set of a surge tank and a column feeding into the surge tank, wherein the ammonia component in the ammonia vapor is transferred into the aqueous solution by flowing the ammonia vapor through the column while the water is circulated from the surge tank through the column.

13. A system according to claim 12, wherein the water is circulated through the column in a first direction and the ammonia vapor is directed into the column in a second direction, which is opposite to the first direction.

14. A system according to claim 6, wherein the ammonia absorption unit receives the ammonia vapor from the ammonia stripper and absorbs the ammonia component into an acidic aqueous solution.

15. The system according to claim 6, wherein said animal, vegetable, and food byproducts have a total Kjeldahl nitrogen content of at least about 2700 mg/L.

16. The system according to claim 6, wherein said animal, vegetable, and food byproducts have a fat, oil and grease content of at least about 0.6%.