초록 ▼

A system and method for providing an integrated indirectly fired reactor and steam generator are disclosed. According to one embodiment, the reactor comprises an indirect heating zone heating water and generating steam, a mixing zone mixing feedstock and the steam and providing a mixture of the feed

A system and method for providing an integrated indirectly fired reactor and steam generator are disclosed. According to one embodiment, the reactor comprises an indirect heating zone heating water and generating steam, a mixing zone mixing feedstock and the steam and providing a mixture of the feedstock and the steam, and a reaction zone comprising a first reactor and a second reactor. The first reactor converts the mixture to a first syngas at a first temperature. The second reactor converts the first syngas to a second syngas at a second temperature, the second temperature being higher than the first temperature.

대표청구항 ▼

1. A method for providing oxygen-free gasification in a system, comprising: combusting syngas with air in an indirect heating zone to generate hot combustion gases, the indirect heating zone having a heat exchanger for generating steam by using the hot combustion gases;heating a reaction zone by usi

1. A method for providing oxygen-free gasification in a system, comprising: combusting syngas with air in an indirect heating zone to generate hot combustion gases, the indirect heating zone having a heat exchanger for generating steam by using the hot combustion gases;heating a reaction zone by using the hot combustion gases for heating a reaction zone;mixing feedstock and the steam in a mixing zone; providing, by the mixing zone, a mixture of the feedstock and the steam; andperforming oxygen-free gasification in the reaction zone, wherein oxygen-free gasification comprisesconverting, in a first reactor, the mixture to a first syngas at a first temperature; and converting, in a second reactor, the first syngas to a second syngas at a secondtemperature, the second temperature being higher than the first temperature, wherein the hot combustion gases remain separated from the steam, the feedstock, the mixture, the first syngas, and the second syngas. 2. The method of claim 1, wherein the reaction zone is surrounded by the heating zone. 3. The method of claim 1, wherein the first reactor is one of a cylindrical shape or a rectangular shape. 4. The method of claim 1, wherein the first reactor and the second reactor are vertically disposed next to each other and are separated by a dividing wall. 5. The method of claim 1, wherein a plurality of thermal conductors extends from the heating zone to the first reactor and the second reactor. 6. The method of claim 1, wherein the heating zone comprises a first heating zone disposed adjacent to the first reactor and a second heating zone disposed adjacent to the second reactor. 7. The method of claim 1, wherein the mixing zone comprises a feed injection zone and the feedstock is gravity-fed via the feed injection zone. 8. The method of claim 1, further comprising mixing the feedstock with CO2. 9. The method of claim 1, further comprising mixing the feedstock with the steam in the mixing zone in a cross-flow pattern. 10. The method of claim 1, further comprising providing the steam in the form of jets and creating turbulence in mixing zone. 11. The method of claim 1, further comprising collecting, by a compartmentalized recovery zone, residual solid, liquid, or gas generated in the reaction zone. 12. The method of claim 11, wherein the recovery zone comprises an inner compartment and an outer compartment, and wherein air in the outer compartment is evacuated prior to opening the inner compartment to prevent the air from entering the reaction zone. 13. The method of claim 1, wherein a refractory brick lining surrounds the first or second reactor. 14. The method of claim 13, wherein a thermal radiation shield is disposed between the refractory brick lining and the heating zone. 15. The method of claim 1, wherein the second syngas comprises CO2. 16. The method of claim 15, wherein the CO2 is fed for capture and sequestration. 17. The method of claim 15, wherein the second syngas further comprises hydrogen sulfide. 18. The method of claim 17, further comprising extracting the hydrogen sulfide from the second syngas. 19. The method of claim 17, further comprising driving a turbine for power generation by using the second syngas. 20. The method of claim 1, wherein the feedstock is biomass. 21. The method of claim 20, wherein the system further comprising a compressor and an alcohol synthesis reactor. 22. The method of claim 20, further comprising producing, by a distiller, ethanol from the syngas. 23. The method of claim 1, further comprising feeding the second syngas to a synthesis reactor to generate synthetic fuels.