Condensate and feedwater system of steam power plant and operation method for the same
A condensate and feedwater system includes: a deaerator circulation pump that returns condensate water flowing out from a deaerator to a part of a condensate line between a heater and the deaerator; an apparatus to be supplied with part of the condensate water flowing from the heater toward the deaerator, through a supply line branched from the condensate line; a supply line shutoff valve that switches between communication and interruption of the supply line; and a controller that controls opening/closing of the supply line shutoff valve and driving/stopping of the deaerator circulation pump. The controller closes the supply line shutoff valve from an open state at normal operation and at least temporarily drives the deaerator circulation pump from a stopped state at normal operation, in condenser throttling in which supply of extraction steam of a steam turbine to the heater and the deaerator is reduced as compared to that at normal operation and a deaerator water level control valve is closed.
1. A condensate and feedwater system of a steam power plant, comprising:
a deaerator that heats and deaerates condensate water generated in a condenser, by extraction steam of a steam turbine, and temporarily stores the heated and deaerated condensate water;
a heater disposed on a condensate line between the condenser and the deaerator, the heater being configured to heat the condensate water generated in the condenser, by extraction steam of the steam turbine;
a deaerator water level control valve disposed on an upstream side of the heater in the condensate line, the deaerator water level control valve being capable of controlling water level of the condensate water in the deaerator;
a deaerator circulation pump that returns condensate water flowing out from the deaerator to a part of the condensate line between the heater and the deaerator;
an apparatus configured to be supplied with part of the condensate water flowing from the heater toward the deaerator, through a supply line branched from the condensate line;
a supply line shutoff valve disposed on the supply line, the supply line shutoff valve being configured to switch between communication and interruption of the supply line; and
a controller that controls opening/closing of the supply line shutoff valve and controls driving/stopping of the deaerator circulation pump, wherein
the controller
puts the supply line shutoff valve into an open state and puts the deaerator circulation pump into a stopped state, in normal operation, and
closes the supply line shutoff valve from the open state at the normal operation and at least temporarily drives the deaerator circulation pump from the stopped state at the normal operation, in condensate throttling in which supply of the extraction steam to the heater and the deaerator is reduced as compared to that at the normal operation and the deaerator water level control valve is closed.
2. The condensate and feedwater system of the steam power plant according to claim 1 , wherein
the controller starts outputting of a driving command signal to the deaerator circulation pump when a closure detection signal indicating that completion of a transfer from the open state to a closed state of the supply line shutoff valve is detected is inputted from the supply line shutof valve, in the condensate throttling.
3. The condensate and feedwater system of the steam power plant according to claim 1 , wherein
the controller measures lapse time from start of outputting of a closure command signal to the supply line shutoff valve, and starts outputting of a driving command signal to the deaerator circulation pump when the lapse time measured exceeds a preset time, in the condensate throttling.
4. The condensate and feedwater system of the steam power plant according to claim 1 , wherein
the controller starts outputting of a driving command signal to the deaerator circulation pump concurrently with start of outputting of a closure command signal to the supply line shutoff valve, in the condensate throttling.
5. The condensate and feedwater system of the steam power plant according to claim 1 , wherein
the controller continues driving of the deaerator circulation pump throughout the condensate throttling.
6. The condensate and feedwater system of the steam power plant according to claim 1 , wherein
the controller measures lapse time from start of outputting of a driving command signal to the deaerator circulation pump, and either starts outputting of a stopping command signal to the deaerator circulation pump or stops outputting of the driving command signal when the lapse time measured exceeds a preset time, in the condensate throttling.
7. An operation method for a condensate and feedwater system of a steam power plant, the condensate and feedwater system including:
a deaerator that heats and deaerates condensate water generated in a condenser, by extraction steam of a steam turbine, and temporarily stores the heated and deaerated condensate water;
a heater disposed on a condensate line between the condenser and the deaerator, the heater being configured to heat the condensate water generated in the condenser, by extraction steam of the steam turbine;
a deaerator water level control valve disposed on an upstream side of the heater in the condensate line, the deaerator water level control valve being capable of controlling water level of the condensate water in the deaerator;
a deaerator circulation system that returns condensate water flowing out from the deaerator to a part of the condensate line between the heater and the deaerator;
an apparatus configured to be supplied with part of the condensate water flowing from the heater toward the deaerator, through a supply line branched from the condensate line; and
a supply line shutoff valve configured to switch between communication and interruption of the supply line, the operation method comprising:
when switching from normal operation to condensate throttling in which supply of the extraction steam to the heater and the deaerator is reduced as compared to that at the normal operation and the deaerator water level control valve is closed,
closing the supply line shutoff valve from an open state at the normal operation; and
at least temporarily driving the deaerator circulation system from a stopped state at the normal operation.
8. The operation method for the condensate and feedwater system of the steam power plant according to claim 7 , wherein
in the condensate throttling, the deaerator circulation system is started after completion of transfer from the open state to the closed state of the supply line shutoff valve.
9. The operation method for the condensate and feedwater system of the steam power plant according to claim 7 , wherein
in the condensate throttling, the deaerator circulation system is started after a lapse of a preset time from start of closing of the supply line shutoff valve.
10. The operation method for the condensate and feedwater system of the steam power plant according to claim 7 , wherein
in the condensate throttling, the deaerator circulation system is started concurrently with start of a closing operation of the supply line shutoff valve.
11. The operation method for the condensate and feedwater system of the steam power plant according to claim 7 , wherein
the deaerator circulation system continues being driven throughout the condensate throttling.
12. The operation method for the condensate and feedwater system of the steam power plant according to claim 7 , wherein
in the condensate throttling, the deaerator circulation system is stopped after a lapse of a preset time from start of its driving.