Apparatus and method for combusting a fuel at high pressure and high temperature, and associated system and device

1. An energy generation system, comprising:

a combustor apparatus, including:

a mixing arrangement configured to mix a carbonaceous fuel with enriched oxygen and a working fluid from a working fluid source to form a fuel mixture; and

a combustion chamber defined by a porous wall of an inner transpiration member of a porous material, the inner transpiration member being at least partially surrounded by a pressure containment member defining second transpiration fluid supply passages, the inner transpiration member defining the combustion chamber further being substantially cylindrical and having an inlet portion and an opposing outlet portion, the inlet portion of the combustion chamber being configured to receive the fuel mixture for the fuel mixture to be combusted within the combustion chamber at a combustion temperature to form a combustion product, and the inner transpiration member being configured to direct the combustion product along the cylindrical combustion chamber toward the outlet portion, the inner transpiration member further being surrounded by an outer transpiration member disposed between the inner transpiration member and the pressure containment member, the outer transpiration member defining first transpiration fluid supply passages extending therethrough to the inner transpiration member, and the first and second transpiration fluid passages being configured to cooperate to direct a transpiration substance therethrough to the inner transpiration member, the inner transpiration member thereby being configured to receive the transpiration substance externally to the combustion chamber and to direct the transpiration substance about and through a circumference of the porous wall thereof defining the combustion chamber, toward and into the combustion chamber, such that the transpiration substance entering the combustion chamber about the circumference of the porous wall forms a buffer layer immediately adjacent to and about the circumference of the porous wall within the cylindrical combustion chamber, the buffer layer, formed by directing the transpiration substance radially inward from about the circumference of the porous wall within the cylindrical combustion chamber, being configured to buffer interaction between the porous wall and the liquefied incombustible elements and heat associated with the combustion product in the combustion chamber, the transpiration substance and the working fluid each comprising a supercritical carbon dioxide fluid from the working fluid source;

a transformation apparatus configured to receive the combustion product, the transformation apparatus being responsive to the combustion product to transform energy associated therewith into kinetic energy; and

a separator apparatus disposed between the combustor apparatus and the transformation apparatus, the separator apparatus being configured to substantially remove liquefied incombustible elements from the combustion product received thereby prior to the combustion product being directed to the transformation apparatus.

2. A system according to claim 1 , wherein the mixing arrangement is further configured to mix one of a solid carbonaceous fuel, a liquid carbonaceous fuel, and a gaseous carbonaceous fuel with enriched oxygen and the working fluid.

3. A system according to claim 1 , wherein the enriched oxygen comprises oxygen having a molar purity of greater than about 85%.

4. A system according to claim 1 , wherein the carbonaceous fuel is a particulate solid having an average particle size of between about 50 microns and about 200 microns, and the mixing arrangement is further configured to mix the particulate solid carbonaceous fuel with a fluidizing substance comprising one of water and liquid CO 2 having a density of between about 450 kg/m 3 and about 1100 kg/m 3 , the fluidizing substance cooperating with the particulate solid carbonaceous fuel to form a slurry having between about 25 weight % and about 55 weight % of the particulate solid carbonaceous fuel.

5. A system according to claim 1 , wherein the combustion chamber is further configured to receive the fuel mixture in the inlet portion thereof at a pressure of between about 40 bar and about 500 bar.

6. A system according to claim 1 , wherein the transpiration substance is configured to be introduced into the combustion chamber via the transpiration member so as to regulate an exit mixture of the transpiration substance and the combustion product about the outlet portion of the combustion chamber at a temperature of between about 500° C. and about 2000° C.

7. A system according to claim 1 , wherein the combustion temperature is configured such that any incombustible elements in the carbonaceous fuel are liquefied within the combustion product.

8. A system according to claim 1 , wherein the transpiration substance is configured to be introduced into the combustion chamber via the inner transpiration member so as to regulate a mixture of the transpiration substance and the combustion product entering the separator apparatus above a liquefication temperature of the incombustible elements.

9. A system according to claim 8 , further comprising a transpiration substance delivery device disposed subsequently to the separator apparatus and configured to deliver the transpiration substance to the combustion product having the liquefied incombustible elements substantially removed therefrom so as to regulate a mixture of the transpiration substance and the combustion product entering the transformation apparatus at a temperature of between about 500° C. and about 2000° C.

10. A system according to claim 1 , wherein the separator apparatus further comprises a plurality of serially arranged centrifugal separator devices, each centrifugal separator device having a plurality of centrifugal separator elements operably arranged in parallel.

11. A system according to claim 1 , wherein the liquefied incombustible elements removed from the combustion product by the separator apparatus are removably collected in a sump associated with the separator apparatus.

12. A system according to claim 1 , wherein the separator apparatus is configured to be one of housed by the pressure containment member and defined by a pressure-containing housing.

13. A system according to claim 12 , wherein the separator apparatus further comprises a heat-dispersion system operably engaged with the one of the pressure containment member and the pressure-containing housing so as to remove heat therefrom.

14. A system according to claim 13 , wherein the heat-dispersion system comprises a heat transfer jacket having a liquid circulated therein.

15. A system according to claim 1 , wherein surfaces of the separator apparatus exposed to one of the combustion product and the liquefied incombustible elements associated therewith are comprised of a material configured to have at least one of a high temperature resistance, a high corrosion resistance, and a low thermal conductivity.

16. A system according to claim 1 , wherein the combustor apparatus further comprises a heat removal device associated with the pressure containment member and configured to control a temperature thereof, the heat removal device comprising a heat transfer jacket having a liquid circulated therein.

17. A system according to claim 1 , wherein the combustor apparatus is configured such that the combustion product includes greater than about 500 ppm O 2 and less than about 50 ppm CO.

18. A system according to claim 1 , wherein the transformation apparatus comprises a turbine device, the turbine device being responsive to the combustion product so as to transform the energy associated therewith into kinetic energy.

19. A system according to claim 1 , wherein the transformation apparatus further comprises a generator device configured to transform the kinetic energy into electricity.