Method of producing slow-release nitrogenous organic fertilizer from biomass

• US 5,676,727 A
• Filed: 12/07/1995
• Issued: 10/14/1997
• Est. Priority Date: 12/09/1994
• Status: Expired due to Term

• Current Assignee: AST Research, Inc. (Samsung Electronics Co. Ltd.)
• Original Assignee: AST Research, Inc. (Samsung Electronics Co. Ltd.)
• Inventors: Piskorz, Jan K., Radlein, Desmond St. A. G., Majerski, Piotr A.
• Primary Examiner(s): Jones, Deborah
• Assistant Examiner(s): Harding, Amy M.
• Application Number:
  US08/568,549
• Time in Patent Office: 677 Days
• Field of Search: 71/11, 71/12, 71/14, 71/23, 71/25, 71/27
• US Class Current: 71/12
• CPC Class Codes: C05C 11/00 Other nitrogenous fertilisers
• CPC Class Codes: C05C 3/00 Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor
• CPC Class Codes: C05C 9/00 Fertilisers containing urea or urea compounds
• CPC Class Codes: C05F 11/00 Other organic fertilisers
• CPC Class Codes: C05F 11/02 from peat, brown coal, and similar vegetable deposits
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02P 60/21 Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures

Abstract

A process for making organic slow release nitrogenous fertilizers from pyrolysis products obtained from the pyrolysis of biomass uses a chemical reaction to combine a nitrogen compound containing the --NH₂ group with the pyrolysis products to form a mixture. The mixture is heated to form organic nitrogen compounds. Various sources of biomass can be used. The mixture can be heated to remove water and to cause polymerization and solidification to occur. The mixture can also be combined with an absorbent. Previously, nitrogenous fertilizers had been produced using an ammoxidation process requiring long reaction times of up to several hours.

Claims

1. A process for making organic nitrogen compounds suitable for use as a fertilizer, said process comprising:

(a) subjecting at least one material selected from the group consisting of ligno-cellulosic materials and starchy materials to pyrolysis to produce solid, liquid, and vapor products;

(b) chemically combining a nitrogen compound containing an --NH₂ group with said liquid products to form organic nitrogen compounds; and

(c) and recovering the organic nitrogen compounds.

2. A process as claimed in claim 1 wherein step (b) comprises combining said nitrogen compound containing the --NH₂ group with said liquid products to form a mixture and mixing and heating said mixture to form organic nitrogen compounds.

3. A process as claimed in claim 2 wherein the ligno-cellulosic materials and starchy materials are biomass selected from the group consisting of agricultural waste, forestry waste, municipal solid waste, wood, grasses, algae, peat, lignite, food processing waste and beverage processing waste.

4. A process as claimed in claim 3 wherein the nitrogen compound is added during the pyrolysis process.

5. A process as claimed in claim 3 wherein the nitrogen compound is added prior to pyrolysis.

6. A process as claimed in claim 3 wherein the nitrogen compound is added to the liquid products.

7. A process as claimed in any one of claims 1, 2 or 6 wherein the nitrogen compound is added after producing the liquid products.

8. A process as claimed in claim 3 wherein the nitrogen compound is selected from the group consisting of urea, an aqueous solution of urea, an aqueous ammonia solution, ammonia, an amine, an amino-acid, a protein and an ammonium salt.

9. A process as claimed in claim 8 wherein the organic nitrogen compound is added with an absorbent selected from the group consisting of peat, moss, pyrolyric char, charcoal, lignin, manure and finely divided ligno-cellulosic biomass.

10. A process as claimed in claim 9 wherein the organic nitrogen compounds are heated following their formation to remove water.

11. A process as claimed in claim 10 wherein the organic nitrogen compounds are heated to a sufficient temperature to cause polymerization.

12. A process as claimed in claim 11 wherein the organic nitrogen compounds are heated to a sufficient temperature to cause solidification.

13. A process as claimed in any one of claims 1, 2 or 3 wherein the pyrolysis process is carried out at a vapour residence time of less than three seconds.

14. A process as claimed in any one of claims 1, 2 or 3 wherein the pyrolysis process is carried out at a heating rate of at least 1000°

C. per second to a temperature of at least 350°

C.

15. A process as claimed in any one of claims 2, 3 or 4 wherein the mixing and heating take place within a temperature range of approximately 150°

C. to approximately 180°

C.

16. An organic nitrogen compound suitable for use as a fertilizer comprising a chemical mixture of pyrolysis liquid products and a suitable nitrogen compound containing an --NH₂ group.

17. An organic nitrogen compound as claimed in claim 16 wherein the pyrolysis liquid products are formed from biomass selected from the group consisting of agricultural waste, forestry waste, municipal solid waste, wood, grasses, algae, peat, lignite, food processing waste and beverage processing waste.

18. An organic nitrogen compound as claimed in any one of claims 16 or 17 wherein the organic nitrogen compound is a solid.

19. An organic nitrogen compound as claimed in any one of claims 16 or 17 wherein the mixture is combined with an absorbent selected from the group consisting of peat, moss, pyrolyric char, charcoal, lignin, manure and finely divided ligno-cellulosic biomass.