A system that regenerates a lean solvent from a CO 2 rich solvent, comprising: a power generator comprising a high pressure turbine, an intermediate pressure turbine and a low pressure turbine; wherein the power generator is configured to receive a high pressure steam in the high pressure turbine and in the intermediate pressure turbine, to produce a first intermediate pressure steam and a second intermediate pressure steam from the intermediate pressure turbine, and to produce a first low pressure steam from the low pressure turbine, wherein the low pressure turbine receives the first intermediate pressure steam; a boiler feedwater pump turbine configured to produce a second low pressure steam from the second intermediate pressure steam; a fluid conditioning unit configured to receive a first portion of the second low pressure steam and a first portion of the first low pressure steam and produce a conditioned stream; a condenser configured to receive a second portion of the second low pressure steam and a second portion of the first low pressure steam, and to produce a condensate; and a heat exchanger configured to (a) receive the conditioned stream and a CO 2 rich solvent, and (b) produce a lean solvent from the CO 2 rich solvent using the conditioned stream, wherein the fluid conditioning unit comprises a blend station configured to mix at least the first portion of the second low pressure steam and the first portion of the first low pressure steam with a second stream having a pressure that is greater than the first and second low pressure steams (206, 207) but less than the high pressure steam, wherein the second stream comprises a product from at least one of a low pressure turbine, a feedwater heater, and a superheated steam generator; further wherein the condensate is received from the condenser and pumped by a condensate pump, and wherein a condensed conditioned stream is received from the heat exchanger and pumped by the condensate pump. a power generator comprising a high pressure turbine, an intermediate pressure turbine and a low pressure turbine; wherein the power generator is configured to receive a high pressure steam in the high pressure turbine and in the intermediate pressure turbine, to produce a first intermediate pressure steam and a second intermediate pressure steam from the intermediate pressure turbine, and to produce a first low pressure steam from the low pressure turbine, wherein the low pressure turbine receives the first intermediate pressure steam; a boiler feedwater pump turbine configured to produce a second low pressure steam from the second intermediate pressure steam; a fluid conditioning unit configured to receive a first portion of the second low pressure steam and a first portion of the first low pressure steam and produce a conditioned stream; a condenser configured to receive a second portion of the second low pressure steam and a second portion of the first low pressure steam, and to produce a condensate; and a heat exchanger configured to (a) receive the conditioned stream and a CO 2 rich solvent, and (b) produce a lean solvent from the CO 2 rich solvent using the conditioned stream, wherein the fluid conditioning unit comprises a blend station configured to mix at least the first portion of the second low pressure steam and the first portion of the first low pressure steam with a second stream having a pressure that is greater than the first and second low pressure steams (206, 207) but less than the high pressure steam, wherein the second stream comprises a product from at least one of a low pressure turbine, a feedwater heater, and a superheated steam generator; further wherein the condensate is received from the condenser and pumped by a condensate pump, and wherein a condensed conditioned stream is received from the heat exchanger and pumped by the condensate pump.