Method for operating a waste heat steam generator
View Patent ↗A method for operating a waste heat steam generator including an evaporator, an economizer having a number of economizer heating surfaces, and a bypass line connected on the flow medium side in parallel with a number of economizer heating surfaces is provided. The method makes possible higher operational safety and reliability in the control of the waste heat steam generator. For this purpose, a parameter that is characteristic of the thermal energy fed to the waste heat steam generator is used to control or regulate the flow rate of the by-pass line.
1. A method for operating a waste heat steam generator, comprising:
providing the waste heat steam generator with an evaporator, an economizer with a first plurality of economizer heating surfaces, and a bypass line connected in parallel with a second plurality of economizer heating surfaces on a flow medium side; and
using a variable that is characteristic of a thermal energy supplied to the waste heat steam generator to control or regulate a flow rate through the bypass line, and
wherein a power output of a gas turbine connected upstream of the waste heat steam generator on a flue gas side is used as the characteristic variable for the thermal energy supplied to the waste heat steam generator,
wherein a temperature device and pressure device are provided at the inlet to the evaporator in order to respectively measure the temperature and pressure at the inlet to the evaporator,
wherein the temperature device and pressure device at the evaporator inlet are used for controlling or regulating the flow rate through the bypass line,
wherein a saturation temperature in the evaporator, determined from the pressure measurement at the evaporator inlet, is used for controlling or regulating the flow rate through the bypass line, and
wherein as a result of the controlling or regulating the flow rate through the bypass line the temperature at the inlet to the evaporator includes a deviation from the saturation temperature.
2. The method as claimed in claim 1 , wherein when the characteristic variable is increased the flow rate through the bypass line is reduced.
3. The method as claimed in claim 1 , wherein when the characteristic variable is reduced the flow rate through the bypass line is increased.
4. The method as claimed in claim 1 , wherein a temperature at a mixing point at an outlet of the bypass line is used for controlling or regulating the flow rate through the bypass line.
5. A waste heat steam generator having an evaporator, comprising:
an economizer with a first plurality of economizer heating surfaces;
a bypass line connected in parallel with a second plurality of economizer heating surfaces on a flow medium side;
a flow control or flow regulator valve;
a first temperature measuring device and a pressure measuring device at an evaporator inlet;
a second temperature measuring device at a mixing point at an outlet of the bypass line; and
a control device that is connected to the first temperature measuring device and; the second temperature measuring device on an input side, and connected to the flow control or flow regulator valve on an output side,
wherein the control device is embodied for performing a method, the method comprising:
using a variable that is characteristic of a thermal energy supplied to the waste heat steam generator to control or regulate a flow rate through the bypass line,
wherein a power output of a gas turbine connected upstream of the waste heat steam generator on a flue gas side is used as the characteristic variable for the thermal energy supplied to the waste heat steam generator,
wherein the first temperature device and the pressure device at the evaporator inlet are used for controlling or regulating the flow rate through the bypass line,
wherein a saturation temperature in the evaporator, determined from the pressure measurement at the evaporator inlet, is used for controlling or regulating the flow rate through the bypass line, and
wherein as a result of the controlling or regulating the flow rate through the bypass line the temperature at the inlet to the evaporator includes a deviation from the saturation temperature.
6. The steam generator as claimed in claim 5 , wherein when the characteristic variable is increased the flow rate through the bypass line is reduced.
7. The steam generator as claimed in claim 5 , wherein when the characteristic variable is reduced the flow rate through the bypass line is increased.
8. The steam generator as claimed in claim 5 , wherein a temperature at a mixing point at an outlet of the bypass line is used for controlling or regulating the flow rate through the bypass line.
9. A gas and steam turbine system, comprising:
a waste heat steam generator, comprising:
an economizer with a first plurality of economizer heating surfaces;
a bypass line connected in parallel with a second plurality of economizer heating surfaces on the flow medium side;
a flow control or flow regulator valve;
a first temperature measuring device and pressure measuring device at an evaporator inlet;
a second temperature measuring device at a mixing point at an outlet of the bypass line; and
a control device that is connected to the first temperature measuring device, the second temperature measuring device, and the pressure measuring device on an input side, and connected to the flow control or flow regulator valve on an output other side,
wherein the control device is embodied for performing a method, the method comprising:
using a variable that is characteristic of a thermal energy supplied to the waste heat steam generator to control or regulate a flow rate through the bypass line,
wherein a power output of a gas turbine connected upstream of the waste heat steam generator on a flue gas side is used as the characteristic variable for the thermal energy supplied to the waste heat steam generator, and
wherein the first temperature device and the pressure device at the evaporator inlet are used for controlling or regulating the flow rate through the bypass line,
wherein a saturation temperature in the evaporator, determined from the pressure measurement at the evaporator inlet, is used for controlling or regulating the flow rate through the bypass line, and
wherein as a result of the controlling or regulating the flow rate through the bypass line the temperature at the inlet to the evaporator includes a deviation from the saturation temperature.
10. The turbine as claimed in claim 9 , wherein when the characteristic variable is increased the flow rate through the bypass line is reduced.
11. The turbine as claimed in claim 9 , wherein when the characteristic variable is reduced the flow rate through the bypass line is increased.
12. The turbine as claimed in claim 9 , wherein a temperature at a mixing point at an outlet of the bypass line is used for controlling or regulating the flow rate through the bypass line.