Method and system for gasification of biomass

1. A continuous system for gasification of a high ash biomass feedstock, wherein the high ash biomass feedstock comprises primarily farm wastes, comprising:

a fuel conditioning zone including an animal manure dryer and a fuel metering bin;

a reaction zone, the reaction zone including a controllable system for introducing air into the high ash biomass feedstock, the air being introduced at approximately ¼ of a level required for complete oxidation of the high ash biomass feedstock, wherein the reaction zone includes a live floor having multiple augers in a side by side configuration, and wherein a speed of the multiple augers is controlled so that the high ash biomass feedstock is taken away at a rate at which it is introduced;

a char cooling area, the char cooling area having a gas capturing system for recovering gas released by the char in the char cooling area as the char cools and where the char cooling area includes at least one char removal auger, the char removal auger running in a direction transverse to the live floor, wherein the carbon content of the char is adjusted by varying one or more of the feed rate of the fuel and air into the system, and wherein a biochar with high carbon content is produced; and

a controller configured to adjust dwell time of the high ash biomass feedstock in the fuel conditioning zone, the reaction zone, and the char cooling area, and maintain a continuous process.

2. The system of claim 1 , wherein air is introduced into the gasification zone at a level below that required for complete combustion.

3. The system of claim 1 , wherein the gas capturing system of the char cooling area includes a gas return to direct at least a portion of the captured gas to the reaction zone.

4. The system of claim 1 , wherein the high ash biomass feedstock is animal manure.

5. The system of claim 1 , wherein the reaction zone is operated with a gas outlet temperature of about 400 to 600° C.

6. The system of claim 1 , wherein the gas recovered from the char cooling area and from the reaction zone is combusted in a secondary chamber.

7. The system of claim 6 , wherein the secondary chamber is operated with a flue gas outlet temperature of about 1200° C.

8. A continuous system for gasification of a high ash biomass feedstock, wherein the high ash biomass feedstock comprises primarily farm wastes, comprising:

a fuel conditioning zone wherein the high ash biomass feedstock including animal manure is pre-heated, the fuel conditioning zone including a fuel dryer and a fuel metering bin;

a reaction zone, the reaction zone including a controllable system for introducing air into the high ash biomass feedstock, the air being introduced at approximately ¼ of a level required for complete oxidation of the high ash biomass feedstock, the controllable system for introducing air into the biomass further including an auger system having at least two augers positioned side by side to move material evenly across a length and a width of the reaction zone, and wherein a speed of the at least two augers is controlled so that the biomass feedstock is taken away at a rate at which it is introduced;

a char cooling area, the char cooling area having a gas capturing system for recovering gas released by the char in the char cooling area as it cools and from the reaction zone and where the char cooling area includes at least one char removal auger, the char removal auger running in a direction transverse to a live floor, wherein the carbon content of the char is adjusted by varying one or more of the feed rate of the fuel and air into the system, and wherein a biochar with high carbon content is produced;

a chamber wherein the gas recovered from the char cooling area and from the reaction zone is mixed with oxidizer air and oxidized; wherein heat is recovered from a resulting flue gas before admission to the fuel conditioning zone; and

a controller configured to adjust dwell time of the high ash biomass feedstock in the fuel conditioning zone, the reaction zone, the char cooling area and the chamber, and maintain a continuous process.

9. The system of claim 8 , wherein the high ash biomass feedstock is animal manure.

10. The system of claim 8 , wherein the reaction zone is operated with a gas outlet temperature of about 400 to 600° C.

11. The system of claim 8 , wherein the chamber is operated with a flue gas outlet temperature of about 1200° C.

12. A continuous system for gasification of a high ash biomass feedstock, wherein the high ash biomass feedstock comprises primarily farm wastes, comprising:

a fuel conditioning zone wherein the high ash biomass feedstock including animal manure is pre-heated and/or dried, the fuel conditioning zone including a fuel dryer and a fuel metering bin;

a reaction zone, the reaction zone including a controllable system for introducing air into the biomass, the air being introduced at approximately ¼ of a level required for complete oxidation of the high ash biomass feedstock, the controllable system for introducing air into the high ash biomass feedstock further including an auger system having at least two augers positioned side by side to move material evenly across a length and a width of the reaction zone, the auger system also including a transverse auger that runs transverse to the direction of the at least two augers to remove char from the reaction zone, and wherein a speed of the at least two augers is controlled so that the biomass feedstock is taken away at a rate at which it is introduced;

a char cooling area, the char cooling area having a gas capturing system for recovering gas released by the char in the char cooling area as it cools and routing the captured gas to the reaction zone, wherein the carbon content of the char is adjusted by varying one or more of the feed rate of the fuel and air into the system, and wherein a biochar with high carbon content is produced;

a chamber wherein the gas recovered from the char cooling area and from the reaction zone is mixed with oxidizer air and oxidized; wherein heat is recovered from a resulting flue gas before admission to the fuel conditioning zone; and

a controller configured to adjust dwell time of the high ash biomass feedstock in the fuel conditioning zone, the reaction zone, the char cooling area and the chamber, and maintain a continuous process.

13. The system of claim 12 , wherein the high ash biomass feedstock is animal manure.

14. The system of claim 12 , wherein the reaction zone is operated with a gas outlet temperature of about 400 to 600° C.

15. The system of claim 12 , wherein the chamber is operated with a flue gas outlet temperature of about 1200° C.