Granted Patent B2

US 12,371,621 · App. 18/126,563 · Granted Jul 29, 2025

Inventor: Michael McGolden (Evansville, IN)

Assignee: McGolden, LLC

C10B57/10C05F11/00C10B49/04C10B53/00C10J3/30C10J3/723C10L5/42F23G5/027F23J1/02C10J2200/152C10J2200/158C10J2300/0909C10J2300/0916C10J2300/0956F23G2201/40Y02E50/10Y02E50/30Y02P20/145

Abstract

Claims (22)

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

a reaction zone, the reaction zone configured to receive an ash-containing biomass feedstock and including a controllable system for introducing air into the ash-containing biomass feedstock to form a char, the air being introduced at a level less than that required for complete oxidation of the ash-containing biomass feedstock, the reaction zone including a live floor having multiple augers in a side by side configuration, wherein a speed of the multiple augers is controlled to control a rate that material in the reaction zone is transferred through the reaction zone;

a char cooling area, the char cooling area configured to receive the char from the reaction zone and having a gas capturing system for recovering gas released by the char in the char cooling area as the char cools, the char cooling area including at least one char removal auger, wherein the carbon content of the char is adjusted by varying one or more of a feed rate of the ash-containing biomass feedstock and air into the system; and

a controller configured to adjust dwell time of the ash-containing biomass feedstock in 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 reaction zone at a level below that required for complete combustion.

3. The system of claim 1 , further comprising a fuel conditioning zone configured to introduce the ash-containing biomass feedstock to the reaction zone, the fuel conditioning zone including a fuel dryer to preheat the ash-containing biomass feedstock prior to introduction to the reaction zone.

4. The system of claim 3 , wherein the fuel conditioning zone further includes a fuel metering bin.

5. The system of claim 3 , further comprising a chamber wherein the gas recovered from the char cooling area and from the reaction zone is mixed with oxidizer air and oxidized to form a resulting flue gas, wherein heat is recovered from the resulting flue gas before admission to the fuel conditioning zone.

6. 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.

7. The system of claim 1 , wherein the ash-containing biomass feedstock is animal manure.

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 including a fuel dryer and a fuel metering bin, the fuel conditioning zone configured to pre-heat an ash-containing biomass feedstock;

a reaction zone, the reaction zone configured to receive the ash-containing biomass feedstock from the fuel conditioning zone and including a controllable system for introducing air into the ash-containing biomass feedstock to form a char at approximately ¼ of a level required for complete oxidation of the ash-containing biomass feedstock, the reaction zone including a live floor having multiple augers in a side by side configuration, wherein a speed of the multiple augers is controlled to control a rate that material in the reaction zone is transferred through the reaction zone;

a char cooling area, the char cooling area configured to receive the char from the reaction zone and having a gas capturing system for recovering gas released by the char in the char cooling area as the char cools, the char cooling area including at least one char removal auger, wherein the carbon content of the char is adjusted by varying one or more of a feed rate of the ash-containing biomass feedstock and air into the system; and

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

9. The system of claim 8 , wherein air is introduced into the reaction zone at a level below that required for complete combustion.

10. The system of claim 8 , further comprising a chamber wherein the gas recovered from the char cooling area and from the reaction zone is mixed with oxidizer air and oxidized to form a resulting flue gas, wherein heat is recovered from the resulting flue gas before admission to the fuel conditioning zone.

11. The system of claim 8 , 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.

12. The system of claim 8 , wherein the ash-containing biomass feedstock is animal manure.

13. The system of claim 8 , wherein the reaction zone includes a gas outlet temperature of about 400 to 600° C.

14. The system of claim 8 , further comprising a secondary chamber, wherein the gas recovered from the char cooling area and from the reaction zone is combusted in the secondary chamber.

15. The system of claim 14 , wherein the secondary chamber includes a flue gas outlet temperature of about 1200° C.

Continuity (4)

References Cited (50)