An exemplary method for the operation of a CCPP with flue gas recirculation to reduce NOx emissions and/or to increase the CO2 concentration in the flue gases to facilitate CO2 capture from the flue gases as well as a plant designed to operate is disclosed. To allow a high flue gas recirculation ration (rFRG) an imposed combustion inhomogeneity ratio (ri) is used for flame stabilization. The imposed combustion inhomogeneity ratio (ri) is controlled as function of the flue gas recirculation rate (rFRG) and/or combustion pressure. Oxygen or oxygen enriched air to the gas turbine inlet gases or to the combustor is admixed to enhance operatability.

An exemplary method for the operation of a CCPP with flue gas recirculation to reduce NOx emissions and/or to increase the CO2 concentration in the flue gases to facilitate CO2 capture from the flue gases as well as a plant designed to operate is disclosed. To allow a high flue gas recirculation ration (rFRG) an imposed combustion inhomogeneity ratio (ri) is used for flame stabilization. The imposed combustion inhomogeneity ratio (ri) is controlled as function of the flue gas recirculation rate (rFRG) and/or combustion pressure. Oxygen or oxygen enriched air to the gas turbine inlet gases or to the combustor is admixed to enhance operatability.

A thermal power generation system includes a combustor burning oxygen and fuel with supercritical CO.sub.2, a turbine driven by the supercritical CO.sub.2 and water vapor fed from the combustor, a low-pressure supercritical CO.sub.2 storage storing low-pressure supercritical CO.sub.2 from the turbine, a compressor compressing the low-pressure supercritical CO.sub.2, a high-pressure supercritical CO.sub.2 storage storing high-pressure supercritical CO.sub.2 from the compressor, and a high-pressure supercritical CO.sub.2 feeder supplying between the high-pressure supercritical CO.sub.2 storage and the combustor, in which the high-pressure supercritical CO.sub.2 feeder supplies the high-pressure supercritical CO.sub.2 to the combustor at a constant pressure. Thus, the thermal power generation system can perform adjustment of an electric power supply required to use unstable renewable energy sources such as solar and wind power, can achieve high efficiency power generation with high temperature working fluid, and can reduce emissions of environmental load substances such as NO.sub.x and CO.sub.2.

A thermal power generation system includes a combustor burning oxygen and fuel with supercritical CO.sub.2, a turbine driven by the supercritical CO.sub.2 and water vapor fed from the combustor, a low-pressure supercritical CO.sub.2 storage storing low-pressure supercritical CO.sub.2 from the turbine, a compressor compressing the low-pressure supercritical CO.sub.2, a high-pressure supercritical CO.sub.2 storage storing high-pressure supercritical CO.sub.2 from the compressor, and a high-pressure supercritical CO.sub.2 feeder supplying between the high-pressure supercritical CO.sub.2 storage and the combustor, in which the high-pressure supercritical CO.sub.2 feeder supplies the high-pressure supercritical CO.sub.2 to the combustor at a constant pressure. Thus, the thermal power generation system can perform adjustment of an electric power supply required to use unstable renewable energy sources such as solar and wind power, can achieve high efficiency power generation with high temperature working fluid, and can reduce emissions of environmental load substances such as NO.sub.x and CO.sub.2.

Embodiments for inducing swirl upstream of a compressor are provided. In one example, a method includes during a first condition, flowing exhaust gas from downstream of a turbine to upstream of a compressor via a tangential flow duct of an exhaust gas recirculation (EGR) injector circumferentially surrounding an intake passage upstream of the compressor, and during a second condition, flowing exhaust gas from downstream of the turbine to upstream of the compressor via a radial flow duct of the EGR injector.

Embodiments for inducing swirl upstream of a compressor are provided. In one example, a method includes during a first condition, flowing exhaust gas from downstream of a turbine to upstream of a compressor via a tangential flow duct of an exhaust gas recirculation (EGR) injector circumferentially surrounding an intake passage upstream of the compressor, and during a second condition, flowing exhaust gas from downstream of the turbine to upstream of the compressor via a radial flow duct of the EGR injector.

This disclosure relates to the unique integration of a plurality of thermodynamic cycles comprised of a supercritical carbon dioxide thermodynamic cycle, one or more other thermodynamic cycles with multiple heat sources derived from nuclear fuel, solar energy, hydrogen, and fossil fuels, with the energy production systems configured to noticeably improve power plant efficiency, cost and performance.

An enhanced oil recovery method in which carbon dioxide is injected into a well to pressure the well or add lift a production flow from the well recaptures the injected carbon dioxide for reinjection into the well for lift or into another well in a group of for pressuring the well or adding lift to the production flow from the well. Geothermal energy in the production stream can be converted to electrical power for use in the recapturing of the carbon dioxide or other operations at the well site.

A system includes a turbine combustor that includes a head end portion having a head end chamber, a combustion portion having a combustion chamber disposed downstream from the head end chamber, a cap disposed between the head end chamber and the combustion chamber, and a flow distributor configured to distribute an exhaust flow circumferentially around the head end chamber. The flow distributor includes at least one exhaust gas flow path.

A system includes a turbine combustor that includes a head end portion having a head end chamber, a combustion portion having a combustion chamber disposed downstream from the head end chamber, a cap disposed between the head end chamber and the combustion chamber, and a flow distributor configured to distribute an exhaust flow circumferentially around the head end chamber. The flow distributor includes at least one exhaust gas flow path.