Synthetic fuels and chemicals production with in-situ CO
Novel redox based systems for fuel and chemical production with in-situ CO 2 capture are provided. A redox system using one or more chemical intermediates is utilized in conjunction with liquid fuel generation via indirect Fischer-Tropsch synthesis, direct hydrogenation, or pyrolysis. The redox system is used to generate a hydrogen rich stream and/or CO 2 and/or heat for liquid fuel and chemical production. A portion of the byproduct fuels and/or steam from liquid fuel and chemical synthesis is used as part of the feedstock for the redox system.
1. A method for producing a liquid fuel from a solid carbonaceous fuel comprising:
pyrolizing a first portion of the solid carbonaceous fuel to form the liquid fuel; and
indirectly gasifying a second portion of the solid carbonaceous fuel to form separate streams of hydrogen and CO 2 rich gases by:
reducing metal oxide containing particles in a first reaction zone with the second portion of the solid carbonaceous fuel thereby forming the CO 2 rich gases and reduced metal oxide containing particles;
directly sending a first portion of the reduced metal oxide containing particles from the first reaction zone to a second reaction zone, and a second portion of the reduced metal oxide containing particles from the first reaction zone to a third reaction zone;
oxidizing the first portion of the reduced metal oxide containing particles in the second reaction zone with steam thereby generating the hydrogen rich gases and at least partially oxidized metal oxide containing particles;
sending the at least partially oxidized metal oxide containing particles from the second reaction zone to the third reaction zone;
oxidizing the at least partially oxidized metal oxide containing particles from the second reaction zone and the second portion of the reduced metal oxide containing particles from the first reaction zone in the third reaction zone with an oxygen containing gas, thereby generating oxidized metal oxide containing particles; and
returning the oxidized metal oxide containing particles from the third reaction zone to the first reaction zone; and
reacting hydrogen from the hydrogen rich gases with carbon dioxide from the CO 2 rich gases in a CO 2 hydrogenation reaction to form synthetic liquid fuel.
2. The method of claim 1 , where the metal oxide containing particle is an iron oxide containing particle.
3. The method of claim 1 , where the metal oxide containing particles in the first reaction zone form a packed moving bed.
4. The method of claim 1 , where the first reaction zone is operated at a temperature of greater than or equal to 400° C. and less than or equal to 1200° C. and at a pressure of greater than or equal to 1.01×10 5 Pa and less than or equal to 8.10×10 6 Pa.
5. The method of claim 1 , where at least a portion of the carbon dioxide from the CO 2 rich gases is sequestered.
6. The method of claim 1 , where at least a portion of the steam is generated using heat from the CO 2 hydrogenation reaction.