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Systems and a method for controlling a temperature of an exhaust gas stack are provided. The system includes a first heat exchanger positioned upstream in exhaust gas flow communication to an exhaust gas inlet to the stack, a second heat exchanger positioned upstream in exhaust gas flow communicatio

Systems and a method for controlling a temperature of an exhaust gas stack are provided. The system includes a first heat exchanger positioned upstream in exhaust gas flow communication to an exhaust gas inlet to the stack, a second heat exchanger positioned upstream in exhaust gas flow communication to the first heat exchanger, and a water side conduit configured to direct a flow of relatively hot water from the second heat exchanger to the first heat exchanger such that a temperature of a flow of exhaust gas flowing through the first exchanger is maintained within a predetermined range.

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1. A stack temperature control system comprising: a first heat exchanger positioned upstream in exhaust gas flow communication to an exhaust gas inlet to the stack;a second heat exchanger positioned upstream in exhaust gas flow communication to the first heat exchanger; anda water side conduit confi

1. A stack temperature control system comprising: a first heat exchanger positioned upstream in exhaust gas flow communication to an exhaust gas inlet to the stack;a second heat exchanger positioned upstream in exhaust gas flow communication to the first heat exchanger; anda water side conduit configured to direct a flow of relatively hot water from said second heat exchanger to said first heat exchanger such that a temperature of a flow of exhaust gas flowing through said first heat exchanger is maintained within a predetermined range by heat transferred from the flow of relatively hot water from said second heat exchanger to the flow of exhaust gas flowing said first heat exchanger. 2. A system in accordance with claim 1 wherein the flow of exhaust gas flowing through said first heat exchanger is maintained such that a temperature of the flow through said first heat exchanger is maintained greater than at least one of a sulfur dew point temperature and an acid dew point temperature. 3. A system in accordance with claim 1 wherein said second heat exchanger comprises a high pressure economizer of a heat recovery steam generator. 4. A system in accordance with claim 3 wherein said water side conduit comprises a fuel heater and a pressure reducing valve. 5. A system in accordance with claim 1 wherein said second heat exchanger comprises an intermediate pressure economizer of a heat recovery steam generator. 6. A system in accordance with claim 5 wherein said water side conduit comprises a pressure reducing valve and at least one of a water-to-water heat exchanger and a flash tank mixing vessel. 7. A system in accordance with claim 5 wherein said water side conduit comprises a bypass used to control a mass flow rate of water through the first heat exchanger. 8. A method of controlling a temperature of an exhaust gas stack, said method comprising: transferring heat from a flow of exhaust gas to a flow of water in a first heat exchanger; andtransferring heat from the flow of water to the flow of exhaust gas using a second heat exchanger downstream of the first heat exchanger in a direction of the flow of exhaust gas. 9. A method in accordance with claim 8 wherein transferring heat from the flow of water to the flow of exhaust gas using a second heat exchanger comprises transferring heat from the flow of water to the flow of exhaust gas using a low pressure economizer. 10. A method in accordance with claim 8 further comprising reducing a pressure of the flow of water using a pressure reducing valve upstream from the second heat exchanger. 11. A method in accordance with claim 8 wherein transferring heat from a flow of exhaust gas to a flow of water in a first heat exchanger comprises transferring heat from a flow of exhaust gas to a flow of water in a high pressure economizer. 12. A method in accordance with claim 11 further comprising transferring a portion of the heat from the flow of water to a flow of fuel in a fuel heater. 13. A method in accordance with claim 11 further comprising bypassing a portion of the flow of water around the second heat exchanger such that the mass flow rate of water through the second heat exchanger is controlled. 14. A method in accordance with claim 8 wherein transferring heat from a flow of exhaust gas to a flow of water in a first heat exchanger comprises transferring heat from a flow of exhaust gas to a flow of water in an intermediate pressure economizer. 15. A method in accordance with claim 14 further comprising transferring heat from the intermediate pressure economizer to the second heat exchanger using a flash tank mixing device. 16. A method in accordance with claim 14 further comprising circulating water through circuit including a booster pump, a flash tank mixing device, a pressure reducing valve and a water side of the second heat exchanger, the a flash tank mixing device receiving heat from the intermediate pressure economizer. 17. A combined cycle power generation system including at least one gas turbine and at least one steam turbine thermally interconnected through at least one heat recovery steam generator; the combined cycle power generation system comprising: a first heat exchanger positioned upstream in exhaust gas flow communication to a heat recovery steam generator exhaust gas outlet;a second heat exchanger positioned upstream in exhaust gas flow communication to the first heat exchanger; anda water side conduit configured to direct a flow of relatively hot water from said second heat exchanger to said first heat exchanger such that a temperature of a flow of exhaust gas flowing through said first exchanger is facilitated being increased. 18. A system in accordance with claim 17 further comprising a controller configured to: receive a temperature value of the exhaust gases proximate the heat recovery steam generator exhaust gas outlet;compare the received temperature value to a predetermined allowable range of values; andcontrol at least one of a flow rate of the flow of relatively hot water and a temperature of the flow of relatively hot water such that a flow of exhaust gas exiting the heat recovery steam generator exhaust gas outlet is maintained within the predetermined allowable range of values. 19. A system in accordance with claim 17 wherein said controller is configured to control a bypass flow around said first heat exchanger to control a mass flow rate of water through the first heat exchanger. 20. A system in accordance with claim 17 wherein said water side conduit comprises a pressure reducing valve at least one of a water-to-water heat exchanger and a flash tank mixing vessel.