Turbine control valves dynamic interaction

A method for controlling steam admission into a steam turbine, the steam turbine comprising a high pressure casing, at least one reduced pressure casing, and at least one moisture-separator reheater to pull moisture from steam exhausted from the high pressure casing to yield dried steam and reheat the dried steam for admission to the at least one reduced pressure casing, the high pressure casing and the at least one reduced pressure casing comprising corresponding control valves for the steam admission, the corresponding control valves for the at least one reduced pressure casing positioned between the at least one moisture-separator reheater and the at least one reduced pressure casing, the method comprising:

• providing the at least one reduced pressure casing opposing the high pressure casing on a turbine shaft common to both the high pressure casing and the at least one reduced pressure casing;
• at an occurrence of a transient event during an operation of the steam turbine when there is a high volume of steam in the at least one moisture-separator reheater, determining a steam flow demand of the steam turbine, wherein the steam flow demand is determined using parameters that include a rotating speed of the steam turbine, a load of the steam turbine, a live steam pressure of the steam turbine, and a steam turbine operating mode;
• elaborating a high pressure control valve opening setpoint as a function of the determined steam flow demand;
• imposing the elaborated high pressure control valve opening setpoint to high pressure control valves associated with the high pressure casing;
• elaborating a reduced pressure control valve opening setpoint as a function of the determined steam flow demand;
• imposing the elaborated reduced pressure control valve opening setpoint to reduced pressure control valves associated with the at least one reduced pressure casing;
• and
• controlling the high pressure control valve opening setpoint and the reduced pressure control valve opening setpoint during the transient event, wherein the controlling includes continuing the elaborating and imposing of the high pressure control valve opening setpoint and the reduced pressure control valve opening setpoint to avoid overpressure in the at least one moisture-separator reheater during the transient event, wherein during the controlling of the high pressure control valve opening setpoint and the reduced pressure control valve opening setpoint, the reduced pressure control valves are more open than the high pressure control valves to reduce overpressure in the at least one moisture-separator reheater for protection thereof.