Power plant with co2 capture

Abstract

A method is provided for operating a combined cycle power plant having at least one gas turbine, a heat recovery steam generator (HSRG), a steam turbine and a CO2 capture system. The method includes recirculating a first partial flow of flue gases from the HRSG. The method also includes capturing CO2 from a second partial flow of flue gases from the HRSG; and operating a supplementary firing to increase the net power output of the plant and to at least partly compensate the power consumption of the CO2 capture system. A combined cycle power plant is also provided. The plant includes at least one gas turbine, at least one heat recovery steam generator, at least one steam turbine at least one CO 2 capture system, and flue gas recirculation. The plant also includes a low excess air supplementary firing.

What is claimed is: 
     
         1 . A method for operating a combined cycle power plant comprising at least one gas turbine ( 6 ), having a compressor ( 1 ), a combustor ( 4 ) and a turbine ( 7 ), a heat recovery steam generator (HSRG) ( 9 ), a steam turbine ( 13 ), a CO2 capture system ( 18 ), a supplementary firing ( 10 ), which is integrated into the heat recovery steam generator (HSRG) ( 9 ) or installed as a duct firing ( 10 ) in the flue duct from the gas turbine to the heat recovery steam generator (HSRG) ( 9 ), and a flue gas recirculation line, the method comprising:
 mixing ambient air ( 2 ) and the first partial ( 21 ) flow of the flue gases ( 19 ); compressing the mixture of ambient air ( 2 ) and first partial flow ( 21 ); combustion fuel ( 5 ) in the combustor  4 ;   expanding the pressurized hot combustion gasses in a turbine ( 7 );   passing the turbine's hot flue gases through a heat recovery steam generator (HSRG) ( 9 ), which generates steam ( 30 );   splitting the flue gas of the gas turbine into at least two partial flows downstream of the heat recovery steam generator (HSRG) ( 9 );   recirculating a first partial flow ( 21 ) of flue gases ( 19 ) from the HRSG ( 9 ) via the recirculation line to the compressor inlet;   directing a second partial flow ( 20 ) of the flue gases ( 19 ) from the heat recovery steam generator (HSRG) ( 9 ) to the CO2 capture system ( 18 );   capturing CO2 from a second partial flow ( 20 ) of flue gases ( 19 ) from the HRSG ( 9 );   operating the supplementary firing ( 10 ) to increase the net power output of the plant and to at least partly compensate the power consumption of the CO2 capture system ( 18 ); wherein the supplementary firing ( 10 ) comprises burner boxes ( 28 ) arranged traversal, spaced apart in arrays in a cross section of the HRSG inlet ( 33 ) or inside the HRSG, and gas turbine flue gas ( 8 ) passes past the burner boxes ( 28 ) through the passages between burner boxes ( 28 ) while fuel and additional ambient air or oxygen enriched air or oxygen are supplied to the burner boxes ( 28 ) and the flame of the supplementary firing is stabilized in the burner boxes ( 28 ).   
     
     
         2 . The method according to  claim 1 , wherein the first partial flow ( 21 ) is recirculated at recirculation rate, which is controlled at a highest possible recirculation rate under the conditions at which stable complete combustion in the gas turbine ( 6 ) can be maintained and at which a residual oxygen concentration after the gas turbine (GTO2) is sufficient to maintain stable complete combustion of the supplementary firing ( 10 ). 
     
     
         3 . The method according to  claim 2 , wherein a sufficient ambient air flow, and/or oxygen enriched air flow, and/or oxygen flow ( 11 ) is injected into the supplementary firing (lo), such that the recirculation rate can be controlled independently of the oxygen concentration required for stable complete combustion of the supplementary firing ( 10 ). 
     
     
         4 . The method according to  claim 3 , wherein the additional ambient air flow, and/or oxygen enriched air flow, and/or oxygen flow ( 11 ) is a function of the recirculation rate. 
     
     
         5 . The method according to  claim 3 , wherein the additional ambient air flow, and or oxygen enriched air flow, and/or oxygen flow ( 11 ) is a function of the residual oxygen concentration after the gas turbine (GTO2). 
     
     
         6 . The method according to  claim 1 , wherein the additional ambient air flow, and or oxygen enriched air flow, and/or oxygen flow ( 11 ) is a function of the supplementary firing load. 
     
     
         7 . The method according to  claim 3 , wherein the additional ambient air flow, and or oxygen enriched air flow, and/or oxygen flow ( 11 ) is a function of the recirculation rate and or a function of the residual oxygen concentration after the gas turbine and or a function of the supplementary firing load. 
     
     
         8 . The method according to  claim 1 , wherein the additional ambient air flow, and or oxygen enriched air flow, and/or oxygen flow ( 11 ) is preheated by low grade heat from a water steam cycle of the combined cycle power plant, and or the CO2 capture system ( 1   a ), and/or the flue gases. 
     
     
         9 . The method according to  claim 1 , wherein the supplementary firing ( 10 ) is operated to increase the power output for power augmentation during peak demand and to increase its operational flexibility. 
     
     
         10 . A combined cycle power plant comprising at least one gas turbine ( 6 ), a compressor ( 1 ) for compressing inlet gas ( 3 ), a combustor ( 4 ) for combustion of fuel ( 5 ) in with the compressed gas, and a turbine ( 7 ) for expanding pressurized hot gases combustion gas, at least one heat recovery steam generator ( 9 ), downstream of the turbine at least one steam turbine ( 13 ) at least one CO2 capture system ( 18 ), downstream of the heat recovery steam generator (HSRG) ( 9 ), and flue gas recirculation line from heat recovery steam generator (HSRG) ( 9 ) to a compressor inlet, wherein a low excess air supplementary firing ( 10 ), which can be operated in a gas flow with less than 10% oxygen concentration with a stoichiometric ratio below 2, is integrated into the heat recovery steam generator (HSRG) ( 9 ) or installed as a duct firing ( 10 ) in a flue duct from the gas turbine to the heat recovery steam generator (HSRG) ( 9 ) is provided, wherein the supplementary firing ( 10 ) comprises burner boxes ( 28 ), arranged traversal, spaced apart in arrays in a cross section of the HRSG inlet ( 33 ) or inside the HRSG, such that gas turbine flue gas ( 8 ) can pass past the burner boxes ( 28 ) through the passages between burner boxes ( 28 ), and wherein the burner boxes ( 28 ) have an u-shaped cross section which is open do a downstream direction and comprise a fuel gas supply ( 12 ) and additional ambient air or oxygen or oxygen enriched air supply ( 11 ) to the inside of the burner boxes ( 28 ) such that the supplementary firing is stabilized in the burner boxes ( 28 ). 
     
     
         11 . The combined cycle power plant according to  claim 10 , wherein ambient air supply lines, and or oxygen enriched air supply lines, and/or oxygen supply lines to the low excess air supplementary firing ( 10 ) are provided. 
     
     
         12 . The combined cycle power plant according to  claim 10 , further comprising an oxygen enrichment plant and or an air separation unit. 
     
     
         13 . The combined cycle power plant according to  claim 10 , wherein at least one oxygen measurement device is installed to measure oxygen concentrations of inlet gases of a compressor inlet gas ( 2 ) and/or to measure a residual oxygen concentration of hot flue gases of a gas turbine ( 8 ) and/or to measure a residual oxygen concentration of flue gases ( 19 ) from the heat recovery steam generator ( 9 ). 
     
     
         14 . The combined cycle power plant according to  claim 10 , wherein at least one CO2 measurement device is installed to measure a CO2 concentration of inlet gases of a compressor inlet gas ( 2 ) and/or to measure a CO2 concentration of hot flue gases of a gas turbine ( 8 ) and/or to measure a CO2 concentration of flue gases ( 19 ) from the heat recovery steam generator ( 19 ).