Method for operating a steam generator

1. A method for operating a steam generator with a combustion chamber having a plurality of evaporator heating surfaces which are connected in a parallel manner on the flow medium side, comprising:

forming a peripheral wall of the combustion chamber of steam generator pipes;

forming an inner wall and a further inner wall at least partly from additional steam generator pipes;

arranging the inner wall and the further inner wall inside the combustion chamber;

connecting the further inner wall downstream from the inner wall on a flow medium side by an intermediate collector;

supplying a flow medium to a first inlet of a first evaporator heating surface at a lower temperature than to a second inlet of a second evaporator heating surface,

wherein a preheater is connected upstream of the first and second inlets on the flow medium side,

wherein a bypass line is arranged so that a first part of the flow medium is conducted to bypass the preheater,

wherein a branch point is provided upstream of the preheater on the flow medium side such that the first part originates at the branch point and bypasses the preheater,

wherein the first part of the flow medium is mixed with a second part of the flow medium that is branched downstream of the preheater on the flow medium side, the mixture of the first part and the second part is supplied to the first inlet, and

wherein the mass throughflow of the first part flow is regulated via a throughflow regulating valve disposed in the bypass line based on thermodynamic characteristics at a measurement point downstream of the first inlet of the first evaporator heating surface,

wherein the measurement point is disposed in the intermediate collector connected downstream of the first evaporator heating surface.

2. The method as claimed in claim 1 , wherein a mass throughflow of the second part flow has an upper limit.

3. The method as claimed in claim 1 , wherein pressure and temperature are used as thermodynamic characteristics, with the saturated steam temperature being determined from the measured pressure and the actual subcooling value being determined based on the measured temperature.

4. The method as claimed in claim 3 ,

wherein a setpoint value is predefined for subcooling, and

wherein the mass throughflow of the first part flow is regulated based on the deviation between the actual and setpoint values for subcooling.

5. The method as claimed in claim 4 , wherein when the actual value for subcooling is lower than the setpoint value, the mass throughflow of the first part flow is increased.

6. The method as claimed in claim 1 ,

wherein the mass throughflow of the second part flow is regulated based on the mass throughflow of the flow medium supplied to the first evaporator heating surface.

7. The method as claimed in claim 1 ,

wherein the flow of the medium supplied to the first evaporator heating surface is regulated based on the outlet enthalpy of a last evaporator heating surface connected downstream of the first evaporator heating surface on the flow medium side.

8. The method as claimed in claim 7 , wherein the outlet enthalpy of the evaporator heating surface is determined based on the temperature at the outlet of the flow medium at the last evaporator heating surface connected downstream of the first evaporator heating surface on the flow medium side and the pressure in a water/steam separator connected downstream of the first, second, and last evaporator heating surfaces on the flow medium side.

9. A steam generator, comprising

means for executing the method as claimed in claim 1 .