Biochar compositions and methods of use thereof
The invention provides for methods, devices, and systems for pyrolyzing biomass. A pyrolysis unit can be used for the pyrolysis of biomass to form gas, liquid, and solid products. The biomass materials can be selected such that an enhanced biochar is formed after pyrolysis. The biomass can be pyrolyzed under specified conditions such that a selected biochar core is formed. The pyrolysis process can form a stable biochar core that is inert and/or resistant to degradation. The biochar or biochar core can be functionalized to form a functionalized biochar or functionalized biochar core. Functionalized can include post-pyrolysis treatments such as supplementation with microbes or physical transformations including annealing and/or activation.
1. A method for preparing a soil amendment comprising:
providing a biomass to a pyrolysis unit;
pyrolyzing the biomass in the pyrolysis unit to produce a stable biochar core that has a rate of degradation that is less than 2.5% per year, wherein the biomass is pyrolyzed at a heating rate from 0.01° C./second up to 1000° C./second and at least one of (i) a temperature greater than 250° C. and (ii) a heating time greater than 0.001 days; and
using the stable biochar to form a soil amendment for placement in a soil bed, wherein the soil amendment has a total phosphorus and a total nitrogen content that provides a concentration of available phosphorus and available nitrogen suitable to promote growth of an organism in the soil bed, which concentration of available phosphorus is at least about 1 part per million (ppm) and available nitrogen is at least about 1 ppm.
2. The method of claim 1 , wherein the available phosphorus provided by the soil amendment is between about 5-1000 ppm and the available nitrogen provided by the biochar is between about 15-10000 ppm.
3. The method of claim 1 , wherein the soil amendment has a selected air filled porosity that is greater than about 10% and a selected water holding capacity that is greater than about 20%.
4. The method of claim 1 , wherein the biomass is pyrolyzed under (i) a heating rate between about 0.1° C./second and 50° C./second, (ii) a temperature greater than about 250° C., and (iii) a heating time greater than about 0.1 days.
5. The method of claim 1 , wherein the biochar core is treated with a wetting agent.
6. The method of claim 1 , wherein the biochar core is mixed with soil or with coconut coir to form the soil amendment.
7. The method of claim 1 , wherein the biochar is pH adjusted to a pH less than about 6 using AlSO 4 .
8. The method of claim 1 , wherein the soil amendment is used in conjunction with an irrigation system.
9. The method of claim 8 , wherein the soil amendment is positioned in a layer that is about 3 inches away from an irrigation system.
10. The method of claim 8 , wherein the soil amendment is positioned below an irrigation system in a layer that is about 4 inches thick.
11. The method of claim 1 , wherein the stable biochar has increased capacity to hold a nutrient or microbial inoculant.
12. The method of claim 1 , wherein the pyrolysis unit is a gasifier.
13. The method of claim 1 , wherein using the stable biochar to form the soil amendment comprises contacting the biochar core with a supplement to produce a functionalized biochar core, which supplement includes a nutrient or biological energy source that enables growth of an organism in the soil bed.
14. The method of claim 1 , wherein the heating rate is controlled to within 20° C. per second.
15. The method of claim 1 , wherein the temperature is controlled to within 20° C.
16. The method of claim 1 , wherein the heating time is greater than or equal to 0.01 days.
17. The method of claim 16 , wherein the heating time is greater than or equal to 0.1 days.
18. The method of claim 1 , wherein the heating rate is from 0.1° C./second up to 1000° C./second.
19. The method of claim 18 , wherein the heating rate is from 1° C./second up to 1000° C./second.
20. The method of claim 1 , wherein the biomass is pyrolyzed at a heating rate from 0.01° C./second up to 1000° C./second and (i) a temperature greater than 250° C. and (ii) a heating time greater than 0.001 days.
21. The method of claim 1 , wherein the concentration of available phosphorus is at least about 5 ppm and available nitrogen is at least about 15 ppm.