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Processes, systems and equipment can be used to convert carbonaceous fuel to an output gas stream that includes CO as a primary C-containing product. In some embodiments, the processes and systems also can produce H2 in a separate reaction, with the H2 advantageously being capable of being combined

Processes, systems and equipment can be used to convert carbonaceous fuel to an output gas stream that includes CO as a primary C-containing product. In some embodiments, the processes and systems also can produce H2 in a separate reaction, with the H2 advantageously being capable of being combined with the CO from a partial oxidation process to provide syngas which, in turn, can be used to produce fuels and chemicals. The processes and systems can be tuned so as to not produce significant amounts of CO2 and do not require an air separation unit.

대표청구항 ▼

1. A method for providing, in a chemical looping system which employs particles that comprise an oxide of a metal having multiple oxidation states, said system comprising an oxidation bed reactor and a fuel conversion reactor, from a carbonaceous fuel a gaseous output that comprises CO as a primary

1. A method for providing, in a chemical looping system which employs particles that comprise an oxide of a metal having multiple oxidation states, said system comprising an oxidation bed reactor and a fuel conversion reactor, from a carbonaceous fuel a gaseous output that comprises CO as a primary carbon-containing product, said method comprising contacting said carbonaceous fuel with particles provided directly from said oxidation bed reactor to said fuel conversion reactor, said contacting occurring in said fuel conversion reactor with a generally co-current flow pattern, whereby oxidized metal in said particles is reduced to a lower oxidation state, thereby providing said gaseous output, transporting the reduced particles from said fuel conversion reactor to said oxidation bed reactor, and contacting said particles with an oxygen-containing gas stream so as to oxidize said metal. 2. The method of claim 1 wherein said particles exiting said fuel conversion reactor are transported to separate bed reactor prior to returning to said oxidation bed reactor, wherein steam is introduced into said bed reactor so as to provide H2 particles that comprise a metal oxide with said metal in an oxidation state intermediate that of said metal upon entry of said particles to and exit of said particles from said fuel conversion reactor. 3. The method of claim 2 wherein said H2 is combined with CO in said gaseous output from said fuel conversion reactor so as to provide syngas. 4. The method of claim 1 further comprising subjecting a portion of said CO to a water gas shift reaction to provide CO2 and H2 and combining the resulting H2 with another portion of said CO so as to provide syngas. 5. The method of claim 4 further comprising directing syngas to a gas separating unit for separating the syngas into its constituent components. 6. The method of claim 4 further comprising subjecting said CO and said H2 to a Fischer-Tropsch process reactor to produce organic fluids. 7. The method of claim 1 further comprising introducing CO2 into said fuel conversion reactor so as to promote production of CO via a Boudouard reaction. 8. The method of claim 1 further comprising subjecting said CO to a water gas shift reaction and recovering the resulting hydrogen. 9. The method of claim 1 further comprising subjecting a portion of said CO to a water gas shift reaction and subjecting the resulting carbon dioxide to a hydrogenation reaction. 10. The method of claim 1 further comprising directing said gaseous output to a gas turbine. 11. The method of claim 1 wherein said carbonaceous fuel comprises a particulate solid. 12. The method of claim 11 wherein said particulate solid comprises pulverized coal. 13. The method of claim 1 wherein said metal oxide particles are iron oxides in a porous composite. 14. The method of claim 1 wherein the CO:CO2 ratio of said gaseous output is at least 60:40. 15. The method of claim 14 wherein the CO:CO2 ratio of said gaseous output is at least 65:35. 16. The method of claim 1 wherein said contacting step occurs in a moving packed bed of said particles. 17. The method of claim 1 wherein said contacting step occurs in a fluidized bed reactor comprising multiple zones, said metal oxide particles and said carbonaceous fuel flowing in the same direction while moving through said zones. 18. The method of claim 16 wherein movement of particles in said moving packed bed is from top to bottom of said reactor. 19. The method of claim 1 wherein said carbonaceous fuel is other than CO. 20. The method of claim 19 wherein said carbonaceous fuel is pulverized coal. 21. The method of claim 1 wherein said metal having multiple oxidation states has at least q, r and s oxidation states where q