Catalytic conversion of carbonaceous feedstock material into a biochar product

1. A method of converting a carbonaceous feedstock material into a solid carbon product, the method comprising:

receiving an amount of a carbonaceous feedstock material;

applying an amount of a catalyst to the carbonaceous feedstock material, the catalyst comprising a metal salt soluble in water and phosphoric acid in a weight ratio between 1:100 to 1:3 of phosphoric acid to the carbonaceous feedstock material;

heating the carbonaceous feedstock material and the applied catalyst in an anaerobic environment to a temperature of at least 300 C, wherein the phosphoric acid reacts with carbon in the carbonaceous feedstock material and reduces an amount of Oxygen relative to an amount of Carbon in the carbonaceous feedstock material, wherein the heating removes water molecules from the carbonaceous feedstock material and forms anhydrous carbon intermediates, and wherein application of the metal salt activates functional groups in the carbonaceous feedstock material; and

generating, via the heating of the carbonaceous feed stock material, the biochar material comprising mineral ash aromatic carbon groups, and an amount of the metal salt.

2. The method of claim 1 , wherein applying an amount of a catalyst comprises: applying a solution of the phosphoric acid to the carbonaceous feedstock material.

3. The method of claim 2 , further comprising:

recovering the catalyst from the biochar material by soaking the biochar material in water in an amount sufficient to dissolve phosphorus ions into H 3 PO 4 .

4. The method of claim 2 , wherein the phosphoric acid removes oxygen and hydrogen from the carbonaceous feedstock material and creates active bonding sites in the carbonaceous feedstock material for carbon lattices to form.

5. The method of claim 2 , wherein the phosphoric acid lowers or reduces a temperature and an energy threshold for carbonization reactions when the carbonaceous feedstock material is heated.

6. The method of claim 1 , wherein applying an amount of a catalyst comprises phosphoric acid and recovered ash.

7. The method of claim 4 , wherein a maximum temperature for heating the carbonaceous feedstock material and the phosphorus and recovered ash is 650 C.

8. The method of claim 1 , wherein an amount of the catalyst is recovered biomass ash including rare earth and alkaline metals and their oxides.

9. The method of claim 8 , recovering an amount of the rare earth and alkaline metals by washing the generated biochar material with water or acid.

10. The method of claim 1 , wherein the metal salt is iron (III) nitrate.

11. The method of claim 10 , further comprising:

soaking the biochar material in an HCl solution sufficient to dissolve iron ions into FeCl 3 ; and

recovering an amount of the FeCl 3 .

12. The method of claim 1 , wherein the anaerobic environment comprises a positive pressure reactor.

13. The method of claim 1 , wherein a minimum heating rate for heating the carbonaceous feedstock material is 150 C per/second.

14. The method of claim 1 , wherein the carbonaceous feedstock material is received onto a conveyor and the catalyst is applied to the carbonaceous feedstock material while moving on the conveyor.

15. The method of claim 1 , wherein the carbonaceous feedstock material is received into a container and the carbonaceous feedstock material is soaked with the catalyst.

16. The method of claim 1 , wherein metal salt is an iron metal salt comprising iron oxide nanoparticles.

17. The method of claim 1 , wherein the metal salt comprises iron phthalocyanine.

18. The method of claim 1 , wherein the carbonaceous feedstock material is any one of wood, corn stover, rice straw or nut hulls.

19. The method of claim 1 , wherein the application of the metal salt facilitates the formation of double bonds between carbon atoms of the carbonaceous feedstock material.