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The invention concerns a method for energy conversion of solid fuels in particular containing carbon comprising a first step which consists in reacting said fuels in a first energy conversion reactor (2, 20). The invention is characterized in that it comprises a second step which consists in injecti

The invention concerns a method for energy conversion of solid fuels in particular containing carbon comprising a first step which consists in reacting said fuels in a first energy conversion reactor (2, 20). The invention is characterized in that it comprises a second step which consists in injecting oxygen brought to the output of said reactor (2, 20), the reaction of the first step being carried out in at least a circulating fluidized bed (30, 31, 40) and in that the metal oxides circulate between two interconnected circulating fluidized beds (30, 31, 40) converting the fuel and oxidizing the oxides.

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The invention claimed is: 1. A method for effecting the energy conversion of solid fuels containing carbon comprising: reacting the solid fuels with oxygen provided by oxide particles to create flue gases and unconverted compounds in a first oxide reduction reactor having an exit, wherein the first

The invention claimed is: 1. A method for effecting the energy conversion of solid fuels containing carbon comprising: reacting the solid fuels with oxygen provided by oxide particles to create flue gases and unconverted compounds in a first oxide reduction reactor having an exit, wherein the first oxide reduction reactor includes a first circulating fluidized bed; providing the flue gases, oxide particles and unconverted compounds from the exit of the first oxide reduction reactor directly to an inlet duct of a gas-solid separation cyclone, the separation cyclone also having a roof, and an exit, wherein the separation cyclone rotates the flue gases, oxide particles and unconverted compounds to create increase residence time within the cyclone and to separate out the oxide particles and convey the separated oxide particles to an oxide oxidation reactor; injecting oxygen into the separation cyclone of the first oxide reduction reactor to convert unconverted compounds exiting the first oxide reduction reactor; oxidizing the oxide particles in the oxide oxidation reactor, wherein the oxide oxidation reactor includes a second circulating fluidized bed; and circulating the oxide particles between the oxide oxidation reactor and the first oxide reduction reactor for conversion of the fuel and oxidization of the oxide particles. 2. The method of claim 1 wherein the energy conversion of the solid fuels is effected through combustion. 3. The method of claim 1 wherein the oxygen is injected into the inlet duct of the gas-solid separation cyclone that is operatively associated with the first oxide reduction reactor. 4. The method of claim 1 wherein the oxygen is injected through the roof of the gas-solid separation cyclone that is operatively associated with the first oxide reduction reactor. 5. The method of claim 1 wherein the oxygen is injected into the exit of the gas-solid separation cyclone that is operatively associated with the first oxide reduction reactor. 6. The method of claim 1 wherein the energy conversion of the solid fuels is effected through gasification. 7. The method of claim 6 wherein the energy conversion of the solid fuels is effected through gasification in a thermochemical cycle. 8. The method of claim 6 wherein the oxygen is injected through the roof of the gas-solid separation cyclone that is operatively associated with the first oxide reduction reactor. 9. The method of claim 8 wherein the oxygen is injected through the roof substantially at the center of the gas-solid separation cyclone that is operatively associated with the first oxide reduction reactor. 10. The method of claim 1, wherein the oxide particles are metal oxides. 11. The method of claim 1, further including a sixth step of providing a second oxide reduction reactor having a circulating fluidized bed to provide two channels for reaction of the fuel whereby oxide particles from the oxide oxidation reactor circulates to both the first and second reduction reactors, and a seventh step of injecting oxygen in the exit of the second oxide reduction reactor. 12. A method for effecting the energy conversion of solid fuels containing carbon comprising: reacting the solid fuels with oxygen provided by oxide particles to create flue gas and unconverted compounds in a first oxide reduction reactor having an exit, wherein the first oxide reduction reactor includes a first circulating fluidized bed; providing a gas-solid separation cyclone at the exit of the first oxide reduction reactor such that it receives the flue gas, unconverted compounds and oxide particles and separates out the oxide particles and provides increased residence time for reaction of the unconverted compounds; injecting oxygen into the first gas-solid separation cyclone to cause increased conversion of unconverted compounds in the separation cyclone; oxidizing the oxide particles in an oxide oxidation reactor to create flue gas and unconverted compounds, wherein the oxide oxidation reactor includes a second circulating fluidized bed; a circulating oxide particles between the oxide oxidation reactor and the first oxide reduction reactor for conversion of the fuel and oxidization of the oxide particles. 13. The method for effecting the energy conversion of claim 12 further comprising the step of: injecting oxygen into an upper portion of the cyclone to procure additional processing time for the compounds to be converted as they spiral toward a bottom portion. 14. The method for effecting the energy conversion of claim 12 wherein the cyclone has a centerline and a roof, further comprising the step of: injecting oxygen into the center of the roof substantially along the centerline to develop a jet virtually coaxial with the risk of impacting the walls, thereby causing increased conversion of the unconverted compounds. 15. A method for effecting the energy conversion of solid fuels containing carbon comprising: reacting the solid fuels with oxygen provided by oxide particles to create flue gas and unconverted compounds in a first oxide reduction reactor having an exit, wherein the first oxide reduction reactor includes a first circulating fluidized bed; providing a gas-solid separation cyclone having an inlet coupled to the exit of the first oxide reduction reactor such that it receives the flue gas, unconverted compounds and oxide particles, and an exit, the separation cyclone separates out the solid particles and exhausts a gaseous phase out of its outlet with very low solid content and with residual rotation; injecting oxygen into the outlet of the gas-solid separation cyclone to cause increased mixing with the gaseous phase exhausted out of the exit thereby increasing conversion of unconverted compounds; oxidizing the oxide particles in an oxide oxidation reactor to create flue gas and unconverted compounds, wherein the oxide oxidation reactor includes a second circulating fluidized bed; and circulating the oxide particles between the oxide oxidation reactor and the first oxide reduction reactor for conversion of the fuel and oxidization of the oxide particles.