Method for operating a gas turbine and gas turbine for performing the method
View Patent ↗In a method for operating a gas turbine, NOx is removed from the exhaust gases of the gas turbine by means of a selective catalysis device with the addition of NH3. The method achieves an extremely low NOx content while simultaneously achieving economic consumption of NH3 and avoiding NH3 in the exhaust gas by maintaining the NOx content of the exhaust gas at a constant level via a regulated return of a portion of the exhaust gas in varying operating conditions of the gas turbine, and by adjusting the addition of the NH3 in the selective catalysis device to the constant NOx level.
1. A method for operating a gas turbine, in which NOx is removed from the flue gases of the gas turbine by means of a selective catalysis device with addition of NH 3 , the method comprising:
keeping NOx content of the flue gases at a constant level by a controlled recirculation of part of the flue gases during changing operating conditions of the gas turbine by:
detecting changes in the NOx content of the flue gas via at least one NOx sensor positioned upstream of the selective catalysis device;
controlling a blower to control flue gas recirculation within the gas turbine; and
adjusting the addition of the NH 3 in the selective catalysis device based on the detected changes in the NOx content of the flue gas to match the addition of NH 3 in the selective catalysis device to the constant level of the NOx content to keep the NOx content of the flue gas at the constant NOx level.
2. The method as claimed in claim 1 , wherein the NOx content of the flue gases originating in the gas turbine and removed therefrom is at the same time reduced in the long term by the flue gas recirculation.
3. The method as claimed in claim 1 , further comprising feeding the flue gases through a cooling device before the selective catalytic reduction in the selective catalysis device.
4. The method as claimed in claim 3 , wherein the cooling device is operated with a direct contact cooler.
5. The method as claimed in claim 3 , wherein the pH and the addition of additives and of oxidants is controlled in the cooling device.
6. The method as claimed in claim 5 , wherein NaOCl and/or O 3 and/or H 2 O 2 are used as the oxidants.
7. The method as claimed in claim 4 , wherein the direct contact cooler is arranged upstream of a separation of the flue gases, and is operatively connected to the entire flue gas mass flow.
8. A gas turbine for carrying out the method of claim 1 , the gas turbine having the selective catalysis device which operates using the NH 3 for removing NOx from the flue gas of the gas turbine, the gas turbine also comprising a controlled flue gas recirculation system and a controller, the controller communicatively connected to a blower of the controlled flue gas recirculation system to control flue gas recirculation and is also configured to control the adjusting of the addition of the NH 3 in the selective catalysis device.
9. The gas turbine as claimed in claim 8 , wherein the flue gas recirculation system is designed to return flue gas to an inlet of the gas turbine.
10. The gas turbine as claimed in claim 8 , further comprising a cooling device having a direct contact cooler that is arranged upstream of the selective catalysis device.
11. The gas turbine as claimed in claim 10 , wherein the cooling device is designed for scrubbing the flue gas.
12. The gas turbine as claimed in claim 8 , wherein the controller controls the flue gas recirculation as a function of the NOx content of the flue pas.
13. The gas turbine as claimed in claim 8 , wherein the gas turbine is equipped with a sequential combustion system.
14. A combined-cycle power plant having a gas turbine as claimed in claim 8 .
15. The method of claim 1 , wherein the keeping of the NOx content of the flue gases at the constant level by the controlled recirculation of part of the flue gases during changing operating conditions of the gas turbine also comprises:
separating the flue gas received from a heat steam generator of a water/steam circuit to direct part of the flue gas to a direct contact cooler;
feeding oxidants into water that is fed into the direct contact cooler to cool and scrub the flue gas within the direct contact cooler; and
directing the flue gas from the direct contact cooler to the selective catalysis device such that the detecting of the changes in the NOx content of the flue gas via the at least one NOx sensor positioned upstream of the selective catalysis device is performed prior to the flue gas from the direct contact cooler being fed into the selective catalysis device.
16. The method of claim 15 , comprising:
emitting flue gas out of the selective catalysis device so the flue gas is released to atmosphere external to the gas turbine.
17. The method of claim 15 , wherein the controlling of the blower to control flue gas recirculation within the gas turbine is performed so that the part of the flue gas that is separated to direct part of the flue gas to the direct contact cooler is adjusted in response to the detected changes in the NOx content of the flue gas.
18. The method of claim 17 , wherein the adjusting of the addition of the NH 3 in the selective catalysis device based on the detected changes in the NOx content of the flue gas to match the addition of NH 3 in the selective catalysis device to the constant level of the NOx content to keep the NOx content of the flue gas at the constant NOx level is controlled by a controller that also controls the blower.
19. The method of claim 18 , comprising:
the at least one NOx sensor communicating with the controller to transmit measurement values to the controller.
20. The method of claim 18 , comprising:
monitoring a ratio of NO to NO 2 in selective catalytic reduction occurring in the selective catalytic device.