초록 ▼

A method of producing syn gas from biomass or other carbonaceous material utilizes a controlled devolatilization reaction in which the temperature of the feed material is maintained at less than 450° F. until most available oxygen is consumed. This minimizes pyrolysis of the feed material. The metho

A method of producing syn gas from biomass or other carbonaceous material utilizes a controlled devolatilization reaction in which the temperature of the feed material is maintained at less than 450° F. until most available oxygen is consumed. This minimizes pyrolysis of the feed material. The method and apparatus utilizes the formed synthesis gas to provide the energy for the necessary gasification. This provides for a high purity syn gas and avoids production of slag.

대표청구항 ▼

1. A method of forming syn gas comprising devolatilizing a feed material in a controlled manner at a first temperature low enough to react oxygen in said feed material without causing pyrolysis thereby forming a char; subsequently combining said char with steam and passing said steam and char throug

1. A method of forming syn gas comprising devolatilizing a feed material in a controlled manner at a first temperature low enough to react oxygen in said feed material without causing pyrolysis thereby forming a char; subsequently combining said char with steam and passing said steam and char through a heated reaction vessel at a second higher temperature to form syn gas.2. The method claimed in claim 1 wherein heat is provided to said heated reaction vessel by combustion of produced syn gas.3. The method claimed in claim 2 wherein said char and steam are forced through said reaction vessel by a cyclone feeder and wherein diluent syn gas is added to said char and steam in said cyclone feeder.4. The method claimed in claim 2 further comprising directing heated air from said combustion of produced syn gas to a feed hopper.5. The method claimed in claim 1 wherein said feed is devolatilized in a series of sealed devolatilization reaction zones and each subsequent devolatilization reaction zone is heated to a higher temperature than the preceding devolatilization reaction zone.6. The method claimed in claim 5 wherein said devolatilization reaction zones are heated by exhaust gas produced by the combustion of produced syn gas wherein said exhaust gas is circulated around the exterior of said devolatilization zones.7. An apparatus to produce syn gas comprising a devolatilization section in communication with a gasification section;wherein said devolatilization section includes a sealable feed material inlet directed towards a plurality of devolatilization zones leading to said gasification section; wherein said gasification section is located in a heated reaction zone; a heater directed to force heated air through said reaction zone; a steam inlet into said reaction zone downstream of said devolatilization section; an exhaust directing said heated air from said reaction zone into indirect contact with said devolatilization section; and a feeder adapted to force reactants through said reaction zone. 8. The apparatus claimed in claim 7 wherein said heater comprises a burner and wherein said burner is connected to a syn gas output line.9. The apparatus claimed in claim 7 wherein said devolatilization section includes a first devolatilization zone in communication with said feed material inlet and a last devolatilization zone in communication with said gasification section.10. The apparatus claimed in claim 9 wherein each of said devolatilization zones includes a rotating auger adapted to direct material from an inlet to an outlet, andwherein said first devolatilization zone communicates with said feed material inlet by a rotating feed mechanism. 11. The apparatus claimed in claim 10 further comprising means to synchronize rotation of said augers and said feed mechanism.12. The apparatus claimed in claim 9 wherein said feeder includes a steam inlet and a char inlet from said last devolatilization reaction zone.13. The apparatus claimed in claim 12 wherein said feeder is a cyclone feeder and said gasification section comprises an elongated reaction coil.14. The apparatus claimed in claim 13 further comprising an eductor adapted to direct produced syn gas to said cyclone feeder to provide required flow velocity in said reaction coils.