KR101638296B1 - Apparatus and method for reactor power control of steam turbine power generation system - Google Patents

Abstract

The present invention relates to a nuclear reactor having a reactor, a high-pressure turbine to which steam is supplied from the reactor through a main combustion engine, a low-pressure turbine to which steam discharged from the high-pressure turbine is supplied via a moisture separator, Pressure turbine, a condenser for condensing the steam discharged from the low-pressure turbine, a plurality of pumps for conveying a plurality of condensed products in the condenser, and a water heater for heating the plurality of condensers, The present invention relates to an output control device for a steam turbine power generation facility including a branch pipe control valve provided in the branch pipe and a control section for controlling the opening degree of the branch pipe control valve.

Description

TECHNICAL FIELD [0001] The present invention relates to an output control apparatus and a control method for a steam turbine power generation facility,

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an output control device and a control method of a steam turbine power generation facility, and more particularly, to an output control device and a control method of a steam turbine power generation plant that follow a demand for output fluctuation by being controlled so as to control a steam flow rate flowing into the turbine .

Power plants using steam turbines are used in thermal power plants and nuclear power plants.

1, the nuclear power plant includes a nuclear reactor 7, turbines 17 and 19, a condenser 21, water heaters 22 and 23, . ≪ / RTI >

The reactor 7 generates steam to be supplied to the turbines 17 and 19 to be described later, including a plurality of fuel rods and a core having a control rod for controlling the reactivity of the reactor core. The control rod regulates the output of the reactor, that is, the core output.

The steam generated in the reactor (7) is supplied to the main steam turbine (14) connected to the reactor (7). The steam supplied to the main engine 14 is supplied to the high pressure turbine 17 through the main engine control valve 16 provided in the main engine 14. The main engine control valve 16 regulates the amount of steam supplied to the high-pressure turbine 17.

The steam supplied to the high-pressure turbine (17) is supplied to the low-pressure turbine (19) via the moisture separator (18). The low pressure turbine 19 is connected to the generator 20.

Pressure turbine 19 is provided with a condenser 21 for condensing the steam discharged from the low-pressure turbine 19 and a low-pressure feedwater heater 22, a feed pump 23, and a high- A water heater 24 is installed. A water supply pipe (15) is connected to the outlet of the high pressure feedwater heater (24).

On the downstream side of the condenser 21, a water supply pipe 15 extending from the condenser 21 to the reactor 7 is connected. A low pressure feedwater heater 22 for heating feedwater sequentially supplied from the condenser 21 and a feed pump 23 for feeding the feedwater to the reactor 7 and a high pressure feedwater heater 24 are disposed.

In the nuclear power plant described above, the steam generated in the reactor is supplied to the high pressure turbine through the main engine, and the turbine is rotated by the steam to rotate the generator connected to the turbine.

The steam discharged from the low pressure turbine is condensed while passing through a condenser, and the condensed condensate is heated by a plurality of stages of feed water heaters installed on the water supply pipe through the water supply pipe and supplied to the reactor again.

On the other hand, consumption of electricity varies greatly depending on season, holiday, weekday, day and night. In the power system, stable voltage and system frequency are maintained by balancing power generation and power consumption.

The output regulation of the power system as a whole is mainly performed by thermal power generation, hydroelectric power generation, etc. However, output control is also required in nuclear power generation.

Conventionally, there has been a risk that cracks in the fuel cladding tube due to thermal fluctuation due to output fluctuation may cause radioactive fission products (xenon, iodine, etc.) on the gas to leak into the reactor coolant.

In recent years, however, nuclear power generation facilities have been undergoing measures such as improvement of cladding pipes, and such concerns have been solved. Researches and tests on power adjustment operation have been carried out by electric power companies, production companies and research institutes. It is designed to be able to operate to adjust the output.

If the power consumption exceeds the production in the power system, the frequency of the generator decreases and the system frequency decreases. When the production exceeds the consumption, the revolution frequency of the generator rises and the system frequency rises. The output control of the power plant corresponding to such fluctuation conditions is usually performed by adjusting the amount of steam generated in the reactor (or the boiler) or adjusting the amount of the main steam supplied to the turbine.

However, the amount of steam generated in the reactor is controlled by controlling the core flow rate and the position of the control rod, and the amount of steam generated in the boiler is also controlled by controlling the amount of water, fuel, and air, The time is big. There is a problem that the tracking ability corresponding to the output fluctuation is deteriorated.

In the method of controlling the amount of main steam supplied to the turbine through the main engine control valve, only the amount of steam supplied to the high-pressure turbine is reduced to reduce the output of the generator. There is a problem that it can not be a proper countermeasure.

SUMMARY OF THE INVENTION It is an object of the present invention to provide an output control apparatus and a control method of a steam turbine power generation facility in which output fluctuation followability is improved in response to a demand for a reduction in output of the generator.

The apparatus for controlling an output of a steam turbine power plant according to an embodiment of the present invention includes a reactor, a high-pressure turbine to which steam is supplied from the reactor through a steam turbine, and a steam discharged from the high- Pressure turbine, a low-pressure turbine, a branch pipe branching from the main engine and connected to the moisture separator, a generator connected to the low-pressure turbine, a condenser for condensing the steam discharged from the low-pressure turbine, a plurality A pump, and a water heater for heating the plurality of steam turbine generators, wherein an output control device of the steam turbine power generation facility comprises: a branch valve provided in the branch pipe; A plurality of pipe control valves provided in a plurality of pipes connecting between the plurality of pumps and the plurality of pumps; A throat control valve provided on a spur gear connected between the feed water heater and the high-pressure turbine; And a control unit for controlling the opening degree of the branch pipe control valve, the plurality of pipe control valves, and the throttle control valve, wherein the control unit measures and analyzes the amount of water stored in the water supply tank and the amount of water stored in the hot water well A plurality of pipe control valves, and a plurality of pipe control valves, or at least two of the valve openings are operated at the same time or at a time difference.

And the control unit controls the opening degree of the branch pipe control valve, the plurality of pipe control valves, and the weight control valve according to an output compensation request signal corresponding to the decrease in output of the generator.

The control section controls the branch pipe control valve to be in any one of a fully opened state, a partially closed state, and a fully closed state.

In addition, the present invention provides a nuclear power plant comprising: a reactor; a high-pressure turbine supplied with steam from the reactor through a main engine; a low-pressure turbine supplied with steam discharged from the high- Pressure turbine, a condenser for condensing the steam discharged from the low-pressure turbine, a plurality of pumps for conveying a plurality of condensed products from the condenser, a water heater for heating the plurality of condensers, A plurality of pipe control valves provided in a plurality of pipes connecting between the plurality of pumps and the plurality of pumps, a weight control valve provided in a weighted engine connected between the water feed heater and the high pressure turbine, A control valve, a plurality of pipe control valves, and a control section for controlling the opening degree of the fuel injection control valve As an output control method for a power plant turbine, (a) step of measuring an output of the generator; (b) comparing the measured output value of the generator with a target output value to determine whether the output is decreased; (c) generating an output compensation request signal corresponding to a decrease in output of the generator; And (d) controlling an amount of steam supplied through the branch pipe in accordance with the output compensation request signal, measuring and analyzing the amount of water stored in the water supply tank and the number of times stored in the hot well of the condensate, Controlling the opening of any one of the control valve and the throttle control valve or interlocking control of two or more of the valve opening simultaneously or at a time difference.

The branch pipe control valve is controlled to be in any one of a fully opened state, a partially closed state, and a fully closed state.

After the step (d), (e) measuring an output of the generator to determine whether the output is compensated; And (f) controlling the branch pipe control valve to be in a state before step (d) according to the output compensation determination.

The step (c) further includes the step (d ') of regulating the amount of return to the plurality of pumps according to the output compensation request signal.

The step (d ') is performed simultaneously with the step (d).

(d ") adjusting the amount of additional steam supplied from the high-pressure turbine to the feedwater heater in accordance with the output compensation request signal.

The step (d ") is performed simultaneously with the step (d).

The present invention also provides a steam turbine comprising a turbine supplied with steam to rotate a generator, a condenser for condensing steam discharged from the turbine, a plurality of pumps for conveying a plurality of condensed products from the condenser, An apparatus for controlling an output of a turbine power generation facility, comprising: a branch control valve provided in a branch branching at a main combustion engine for supplying steam to the turbine and connected to a moisture separator; A plurality of pipe control valves provided in a plurality of pipes connecting the condenser and the plurality of pumps; A throat control valve provided in a spur gear connected to the feed water heater from the turbine; And a control unit for controlling the opening degree of the branch pipe control valve, the plurality of pipe control valves, and the throttle control valve, wherein the control unit measures and analyzes the amount of water stored in the water supply tank and the amount of water stored in the hot water well Wherein the control means controls the opening degree of either one of the branch pipe control valve, the multiple pipe control valve and the weight control valve, or cooperatively controls two or more valve opening at the same time or at a time difference. Of the output control device.

And the control unit controls the opening degree of the branch pipe control valve, the plurality of pipe control valves, and the weight control valve according to an output compensation request signal corresponding to the decrease in output of the generator.

The features and advantages of the present invention will become more apparent from the following detailed description based on the accompanying drawings.

According to the present invention, in order to compensate the output at the time of confirming the output reduction of the generator, it is possible to control not only the steam amount control in the reactor or the boiler having a large time constant but also the control of the increase in the amount of steam flowing into the turbine, The required power reduction control is performed. Such control can be realized by short-time control of the control valve. Therefore, the followability corresponding to the output fluctuation can be greatly improved, and the flowability of the power generation facility can be greatly increased.

1 is a schematic view showing an example of a nuclear power generation facility.
2 is a schematic configuration diagram of a steam turbine power plant including an output control device according to an embodiment of the present invention;
3 is a flowchart illustrating an output control method of a steam turbine power generation facility according to an embodiment of the present invention.
4 is a schematic configuration diagram of a steam turbine power plant including an output control device according to another embodiment of the present invention;

Hereinafter, an output control apparatus and a control method of a steam turbine power generation facility according to an embodiment of the present invention will be described in detail with reference to the accompanying drawings.

In this process, the thicknesses of the lines and the sizes of the components shown in the drawings may be exaggerated for clarity and convenience of explanation.

In addition, the terms described below are defined in consideration of the functions of the present invention, which may vary depending on the intention or custom of the user, the operator. Therefore, definitions of these terms should be made based on the contents throughout this specification.

In addition, the following embodiments are not intended to limit the scope of the present invention, but merely as exemplifications of the constituent elements set forth in the claims of the present invention, and are included in technical ideas throughout the specification of the present invention, Embodiments that include components replaceable as equivalents in the elements may be included within the scope of the present invention.

Hereinafter, an output control apparatus for a steam turbine power generation facility according to an embodiment of the present invention will be described in detail with reference to FIG. 2 is a schematic block diagram of a steam turbine power plant including an output control device according to an embodiment of the present invention.

An example of the power generation facility to which the output control apparatus according to the embodiment of the present invention can be applied may be a nuclear power generation facility 100 as shown in FIG.

The nuclear power generation facility 100 includes a reactor 101, a high pressure turbine 106, a low pressure turbine 111, a moisture separator 107, a generator 112, a condenser 113, a plurality of pumps 116 ), And water feed heaters (118, 121).

The steam generated in the reactor 101 may flow into the high pressure turbine 106 through the main steam pipe 102. The steam generated in the reactor 101 may be steam. The main engine 102 is provided with a main engine control valve 105 at the entrance of the high pressure turbine 106 to control the amount of steam supplied to the high pressure turbine 106 by opening control of the main engine control valve 105.

The steam discharged from the high-pressure turbine 106 is supplied to the low-pressure turbine 111 through the moisture separator 107, which will be described later.

The steam supplied to the high pressure turbine 106 and the low pressure turbine 111 causes the turbine to generate rotational energy and the rotational energy is converted into electric energy by rotating the generator 112 connected to the low pressure turbine 111.

Between the high-pressure turbine 106 and the low-pressure turbine 111, there is provided a moisture separator reheater (MSR) 107 for recovering energy efficiency by separating the moisture from the steam discharged from the high-pressure turbine 106 and heating the steam, .

The moisture separation reheater 107 may include a moisture separator 108 for separating the moisture and a heater for heating the moisture separated from the moisture. At this time, the heater may include a first heater 109 and a second heater 110 so that the steam is sequentially heated.

The heating steam of the first heater 109 may be, for example, the additional steam supplied from the high-pressure turbine 106, and the steam of the second heater 110 may be branched steam branched from the main steam engine 102.

The branch pipe 103 may be formed in the main pipe 102 so that the heating steam can be supplied to the second heater 110. The branch pipe (103) branches from the main pipe (102) and is connected to the second heater (110). Some of the steam supplied through the main engine 102 is supplied to the second heater 110 through the branch pipe 103 and used as heating steam.

The moisture separation and steam heating process through the moisture separation reheater 107 will be described as follows.

The steam at the inlet of the high-pressure turbine 106 is in a moisture vapor state. The steam supplied to the high-pressure turbine 106 operates the turbine to convert the thermal energy of the steam into rotational energy of the turbine.

The steam temperature is lowered, and the humidity of the steam becomes larger at the inlet of the high-pressure turbine 106. As the humidity increases, the loss increases as compared to the dry steam, and corrosion of the turbine blades may occur due to moisture.

In order to solve this problem, the moisture contained in the steam discharged from the high-pressure turbine 106 is separated at the moisture separator 108. The humidity of the exhaust steam of the high-pressure turbine 106 is lowered by the wet separation.

The steam separated by the wet separator 108 is heated by the above-described additional steam and branch steam in the first heater 109 and the second heater 110 to be converted into a dry steam state. The wet steam from which moisture has been removed is supplied to the low-pressure turbine (111).

The steam having rotated the low-pressure turbine 111 is condensed through heat exchange in the condenser 113 to be condensed. The plurality of condensed condensed water in the condenser 113 is stored in a hot well and then supplied to a water heater while being conveyed by a plurality of pumps 116 driven by a motor 117.

The feed water heater may be composed of a low-pressure feedwater heater 118 and a high-pressure feedwater heater 121.

The low-pressure feedwater heater 118 is supplied with a plurality of pulses by a plurality of pumps 116. The plural supplied to the low-pressure feedwater heater 118 by the multiple pump 116 is heated using the low-pressure supplemental steam added from the low-pressure turbine 111 as a heat source.

A first steam engine 122 may be connected between the low-pressure turbine 111 and the low-pressure feedwater heater 118 to supply low-pressure steam to the low-pressure feedwater heater 118. The water supplied through the low-pressure feedwater heater 118 is stored in the water supply tank 119.

The feed water stored in the feed tank 119 is raised by the feed pump 120 and supplied to the high-pressure feedwater heater 121. The feed water supplied to the high-pressure feedwater heater 121 is heated using the high-pressure addition steam from the high-pressure turbine 106 as a heat source. A second steam pipe 124 is connected between the high-pressure turbine 106 and the high-pressure feedwater heater 121 so that high-pressure addition steam is supplied to the high-pressure feedwater heater 121.

The feed water heated by the high-pressure feedwater heater 121 can be supplied to the reactor 101.

Meanwhile, an output control apparatus for a steam turbine power plant according to an embodiment of the present invention includes a branch pipe control valve 104 provided in the branch pipe 103, a control unit 104 for controlling the opening degree of the branch pipe control valve 104, (130).

The branch pipe 103 is a pipe branched from the main pipe 102 and connected to the second heater 110 as described above, and is a pipe for supplying branch steam to the second heater 110. The branch pipe control valve 104 can adjust the amount of branch steam supplied through the branch pipe 103 while the opening degree of the branch pipe control valve 104 is controlled by the control unit 130.

The output information of the generator 112 is transmitted to the control unit 130 in the rated output operation state. At this time, for example, when the decrease of the turbine output occurs, the controller 130 that has obtained the output information of the generator 112 accordingly can generate the output compensation request signal for compensating the decrease output.

The output compensation request signal can be separately generated according to the degree of the output compensation value determined by the controller 130. The output compensation request signal may include a signal for determining the valve position of the branch control valve 104, and the valve position thus determined may be determined by the degree of the output compensation value described above.

The opening degree of the branch pipe control valve 104 is controlled in accordance with the output compensation request signal outputted from the control unit 130 and the branch pipe control valve 104 is closed from the fully open state to the fully closed state according to the valve position determined by the control unit 130 Closed state in a fully opened state, or in a fully closed state in a partially closed state.

However, the branch pipe control valve 104 may be controlled so as to be in either a fully opened state or a fully closed state, although the partial close control may be included as described above.

By controlling the branch pipe control valve 104 to be partially closed or fully closed as described above, the branch steam supplied to the second heater 110 can be partially reduced or completely shut off.

The amount of steam supplied to the high-pressure turbine 106 increases relatively as the amount of steam branched from the main engine 102 is reduced or blocked. As a result, the output of the generator 112 can be increased. The reduced output of the generator is compensated.

The output control of the generator 112 can be performed by controlling the amount of steam supplied to the high-pressure turbine 106 through the branch steam amount control, without controlling the increase / decrease of the steam amount generated in the reactor 101 . Therefore, the tracking ability corresponding to the output fluctuation can be greatly improved.

The output control apparatus according to the present embodiment may further include a plurality of pipe control valves 115. The multiple pipe control valve 115 may be provided on a plurality of pipes 114 connecting between the condenser 113 and the plurality of pumps 116. The opening degree of the multiple-pipe control valve 115 can be controlled in accordance with the output compensation request signal of the control unit 130 described above.

The control unit 130 determines the valve position of the plurality of pipe control valves 115 so that the pipe control valve 115 is closed from the fully closed state to the partially closed state , It is controlled from the fully closed state to the fully closed state, or from the partially closed state to the fully closed state.

Depending on the opening control of the multi-pipe control valve 115 by the control unit 130, the amount of the water flowing into the plurality of pumps 116 may be partially reduced or completely shut off.

By this control, the amount of exhaust steam from the low-pressure turbine 111 can be reduced and the turbine output can be increased.

In addition, the number of pulses to be transferred by the plurality of pumps 116 can be reduced, and the power required by the plurality of pumps 116 can be reduced. As the required power decreases, the motor 117, which drives the plurality of pumps 116, It is possible to reduce the number of revolutions of the motor in comparison with the normal operation, thereby reducing the power consumption. The reduction in power consumption is compensated by the output of the generator 112, resulting in an increase in the output of the generator 112. [

The output control device according to the present embodiment may further include a throat control valve 125.

The throat control valve 125 may be provided in the second spool valve 124 described above. The opening degree of the weight control valve 125 can be controlled in accordance with the output compensation request signal of the control unit 130 described above.

The amount of additional steam supplied to the high-pressure feedwater heater 121 can be partially reduced or completely shut off in accordance with the opening control of the throat-engine control valve 125, so that the amount of steam used for turbine operation within the high- So that the output of the generator 112 can be increased.

If necessary, a thump engine control valve 123 may be further provided in the first throttle valve 122 connecting the low-pressure turbine 111 and the low-pressure feedwater heater 118.

On the other hand, the amount of water stored in the water supply tank 119 and the amount of water stored in the hot well of the condenser may be measured by the measuring unit and transmitted to the controller 130. The control unit 130 analyzes the measured water supply amount and the amount of water to control only the opening degree of one of the branch pipe control valve 104, the multiple pipe control valve 115 and the weight control valve 123 125 Alternatively, two or more valve opening degrees may be controlled at the same time or at a time difference.

In the above description, the high-pressure turbine 106 and the low-pressure turbine 111 are used as the turbine, but the present invention is not limited thereto. A medium pressure turbine may further be included between the high pressure turbine 106 and the low pressure turbine 111.

Hereinafter, a method of controlling an output of a steam turbine power plant according to an embodiment of the present invention will be described with reference to FIGS. 2 and 3. FIG. 3 is a flowchart illustrating an output control method of a steam turbine power plant according to an embodiment of the present invention.

The output control method of the steam turbine power generation facility according to the present embodiment may first perform the step of measuring the output of the generator 112 (S10). The output of the generator 112 may be continuously measured and the measured output information may be transmitted to the controller 130.

Next, the controller 130 may perform a step S21 of comparing the output value of the measured generator 112 with a target output value and a step S22 of determining whether to decrease the output according to the comparison result. In order to perform the output fluctuation control corresponding to the output decrease when the output reduction of the generator 112 is confirmed.

Next, the control unit 130 may perform the step S30 of generating an output compensation request signal corresponding to the decrease in the output of the generator 112 when the output reduction of the generator 112 is confirmed. The output compensation request signal is a signal for controlling the amount of steam supplied to the high pressure turbine 106 to be increased. For example, when the branch steam control valve is provided in the branch pipe 103 as described above, the valve position of the branch steam control valve And a signal to determine the < / RTI >

Next, the controller 130 may output the generated signal to control the amount of branch steam supplied through the branch pipe 103 (S41). More specifically, the control unit 130 controls the opening degree of the branch steam control valve so as to reduce the amount of branch steam supplied to the second heater 110 and increase the amount of steam supplied to the high-pressure turbine 106 can do.

At this time, the branch pipe control valve 104 can be controlled so as to be partially closed from the fully opened state to a fully closed state, or from the partially closed state to the fully closed state.

Alternatively, the control unit 130 may perform the step S42 of outputting the output compensation request signal to control the amount of return to the plurality of pumps 116 (S42). At this time, the output compensation request signal may include a signal for determining the valve position of the plurality of pipe control valves 115 included in the plurality of pipes 114. The control unit 130 may control the opening degree of the pipe control valves 115 Thereby partially reducing or completely shutting down the amount of the water flowing into the plurality of pumps 116.

Alternatively, the control unit 130 may output the above-described output compensation request signal to control the amount of high-pressure addition steam supplied from the high-pressure turbine 106 to the high-pressure feedwater heater 121 or from the low-pressure turbine 111 to the low-pressure feedwater heater 118 It is possible to perform the step S43 of adjusting the supplied low-pressure additional steam amount.

At this time, the output compensation request signal includes a signal for determining the valve position of the throttle control valve 125 provided in the second throttle valve 124 or the throttle control valve 123 provided in the first throttle 122 The control unit 130 may reduce or completely shut off the amount of the additional steam supplied to the high-pressure feedwater heater 121 or the low-pressure feedwater heater 118 by controlling the opening degree of the pump control valves 123 and 125.

Meanwhile, the branch steam amount adjustment step S41, the discharge amount adjustment step S42, and the additional steam amount adjustment step S43 performed by the controller 130 may be performed according to the output compensation request signal output from the controller 130 Only one of them may be performed. Or two or more steps may be performed concurrently or in conjunction in time. In the latter case, however, it is preferable to perform at the same time in order to improve the output fluctuation followability.

The output control method according to the present embodiment may include the steps of measuring the output of the generator 112 after performing the branch steam amount adjustment step S41, the discharge amount adjustment step S42, and the additional steam amount adjustment step S43 Step S50 may be further included.

In this case, the control unit 130 may compare the output value of the measured generator 112 with the target output value (S61) to determine whether output compensation has been performed (S62).

If it is still determined that the output reduction state, i.e., the state where the output compensation is requested, the generation step S30 of the output compensation request signal and the control step thereafter may be performed again.

If it is confirmed that the output is compensated, the controller 130 may perform the step S70 of controlling the branch steam amount, the recovery amount, and the additional steam amount to return to the state before the output compensation request signal is output. That is, the control unit 130 outputs a control signal to return to the open state before the output compensation request signal is output to the branch control valve 104, the multiple pipe control valve 115, and the branch pipe control valves 123 and 125 can do. Thereafter, the output information of the generator 112 can be continuously transmitted to the controller 130, and when the decrease in the output of the generator 112 occurs, the above-described series of control steps can be performed again.

The output control device of the steam turbine power generation facility according to an embodiment of the present invention has been described as being applied to the nuclear power generation facility 100 as an example. However, the follow-up control performed through the opening control of the multiple-pipe control valve 115 or the check valve control valves 123 and 125 when the generator output fluctuates can be applied not only to the nuclear power generation facility 100 but also to the thermal power generation facility.

Hereinafter, an output control apparatus for a steam turbine power generation facility, which can be applied to a thermal power generation plant according to another embodiment of the present invention, will be described with reference to FIG. 4. However, Will be briefly described or omitted below. 4 is a schematic configuration diagram of a steam turbine power generation facility including an output control apparatus according to another embodiment of the present invention.

As shown in the figure, a thermal power generation facility 200 to which an output control apparatus according to the present embodiment can be applied includes a turbine 204 that is supplied with steam and rotates the generator 205, A condenser 206 for condensing the condensed water, a plurality of pumps 207 for conveying condensed water in the condenser 206, and a water heater 208 for heating the plurality of pumps.

The turbine 204 can be supplied with steam from the boiler 201 through the main engine 202 and the main engine control valve 203 is provided in the main engine 202 to control the amount of steam supplied to the turbine 204 .

The thermal energy of the steam supplied to the turbine 204 is converted into rotational energy while rotating the turbine 204, and the generator 205 connected to the turbine 204 is rotated by this rotational energy.

The steam discharged from the turbine 204 is condensed in the condenser 206 and the condensed condensate is supplied to the feedwater heater 208 by a plurality of pumps 207 through the plurality of pipes 209. The additional steam is supplied from the turbine 204 to the feedwater heater 208 through the spindle 211 connecting between the feedwater heater 208 and the turbine 204. The plurality of feeds to the feedwater heater 208 are supplied to the feedwater heater 208, As a heat source.

The water heated in the water feed heater 208 may be supplied to the boiler 201 again.

The thermal power generation facility 200 shown in FIG. 2 differs from the nuclear power generation facility in that no branching structure for supplying branch steam is formed by the wet separation reheater and the wet reheating reheater.

In the drawing, the turbine 204 is composed of one turbine, but is not limited thereto. Pressure turbine and a low-pressure turbine, or may be composed of a high-pressure turbine, a medium-pressure turbine, and a low-pressure turbine.

The output control apparatus according to the present embodiment also includes a plurality of pipe control valves 210 provided in the plurality of pipes 209 and a plurality of pipe control valves 210 provided in the additional pipes 211, Valve 212 may be included.

The multiple pipe control valve 210 and the weight control valve 212 are controlled by the control unit 220 included in the present embodiment.

The control unit 220 can generate an output compensation request signal when output compensation is required when the generator output reduction is confirmed through the measured output information of the generator, ) Or a signal for determining the valve position of the throttling control valve 212.

The opening degree of the multiple-pipe control valve 210 and the weight control valve 212 are controlled in accordance with the output compensation request signal output from the control unit 220, and the amount of steam used for the operation of the turbine 204 is increased Or by reducing the power required in the multiple pump 207, the generator output can be compensated.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, It is obvious that the modification or the modification is possible by the person.

It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.

100: Nuclear power plant 101: Reactor
104: branch control valve 105: main control valve
106: High-pressure turbine 107: Wet separator
111: Low pressure turbine 112: Generator
113: condenser 115: multiple pipe control valve
116: multiple pump 118: low pressure feedwater heater
121: high-pressure feedwater heater 123, 125:
130:
200: Thermal power generation facility 201: Boiler
203: main engine control valve 204: turbine
205: Generator 206:
207: multiple pump 208: feedwater heater
210: multiple pipe control valve 212: pushing control valve

Claims (12)

A high pressure turbine to which steam is supplied from the reactor through the main steam turbine, a low pressure turbine to which steam discharged from the high pressure turbine is supplied through the moisture separation heat exchanger, a steam turbine branched from the steam turbine, Pressure turbine, a condenser for condensing the steam discharged from the low-pressure turbine, a plurality of pumps for conveying a plurality of condensed products in the condenser, and a water heater for heating the plurality of condensers, As an output control device,
A branch valve provided in the branch pipe; And
A plurality of pipe control valves provided in a plurality of pipes connecting the condenser and the plurality of pumps;
A throat control valve provided on a spur gear connected between the feed water heater and the high-pressure turbine; And
And a control section for controlling the opening degree of the branch pipe control valve, the pipe pipe control valve, and the pipe control valve,
Wherein,
The water supply amount measured by the measuring means for measuring the water supply amount stored in the water supply tank storing the water supply water heated by the low-pressure water supply heater and the number of times stored in the hot well of the water supply heater, Wherein the control means controls the opening degree of one of the branch pipe control valve, the multiple pipe control valve and the weight control valve, or interlocks the two or more valve opening means simultaneously or at a time difference,
Wherein the controller is responsive to a decrease in the output of the generator and for determining a valve position of the branch control valve, a signal for determining a valve position of the plurality of pipe control valves, And the opening degree of the branch control valve, the plurality of pipe control valves, and the throttle control valve is controlled in accordance with the output compensation request signal including the signal.
delete The method according to claim 1,
Wherein the control unit controls the branch pipe control valve to be in any one of a fully opened state, a partially closed state, and a fully closed state. A high pressure turbine to which steam is supplied from the reactor through the main steam turbine, a low pressure turbine to which steam discharged from the high pressure turbine is supplied through the moisture separation heat exchanger, a steam turbine branched from the steam turbine, Pressure turbine, a condenser for condensing the steam discharged from the low-pressure turbine, a plurality of pumps for conveying a plurality of condensed products in the condenser, a feed water heater for heating the plurality of condensers, A control valve, a plurality of pipe control valves provided in a plurality of pipes connecting the plurality of pumps and the plurality of pumps, a weight control valve provided in a spur gear connected between the feed water heater and the high-pressure turbine, A pipe control valve, and a control section for controlling an opening degree of the check valve control valve. An output control method,
(a) measuring an output of the generator;
(b) comparing the measured output value of the generator with a target output value to determine whether the output is decreased;
(c) a signal corresponding to a decrease in output of the generator, the signal determining the valve position of the branch control valve, the signal determining the valve position of the plurality of pipe control valves, the signal determining the valve position of the branch control valve Generating an output compensation request signal including the output signal; And
(d) adjusting an amount of steam supplied through the branch pipe in accordance with the output compensation request signal, the amount of water stored in the water supply tank storing the water supply water heated through the low-pressure feedwater heater of the water supply heater, And a controller for analyzing the water supply amount and the return amount transferred to the control unit and for connecting the branch pipe control valve provided in the branch pipe according to the output compensation request signal, A plurality of pipe control valves provided in a plurality of pipes, control means for controlling the opening of any one of the pipe engine control valves provided in the spindle connected between the feed water heater and the high-pressure turbine, Wherein said step of controlling the output of said steam turbine power plant comprises the steps of: The method of claim 4,
Wherein the branch pipe control valve is controlled to be in any one of a fully opened state, a partially closed state, and a fully closed state. The method of claim 4,
After the step (d)
(e) measuring an output of the generator to determine whether output compensation has been performed; And
(f) controlling the branch pipe control valve to be in a state prior to the step (d) when it is confirmed that the output is compensated in the step (e). Way. The method of claim 4,
After the step (c)
further comprising the step of: (d ') adjusting the number of times that the pump is introduced into the plurality of pumps according to the output compensation request signal. The method of claim 7,
Wherein the step (d ') is performed simultaneously with the execution of the step (d). The method of claim 4,
After the step (c)
(d ") adjusting the additional steam amount supplied from the high-pressure turbine to the feedwater heater in accordance with the output compensation request signal. The method of claim 9,
Wherein the step (d ") is performed simultaneously with the execution of step (d). An output of the steam turbine power plant including a turbine supplied with steam to rotate the generator, a condenser for condensing the steam discharged from the turbine, a plurality of pumps for conveying a plurality of condensed products in the condenser, and a water heater for heating the plurality of condensers As a control device,
A branch control valve provided at a branch branching at a main branch for supplying steam to the turbine and connected to the wet scrubber;
A plurality of pipe control valves provided in a plurality of pipes connecting the condenser and the plurality of pumps;
A throat control valve provided in a spur gear connected to the feed water heater from the turbine; And
And a control section for controlling the opening degree of the branch pipe control valve, the pipe pipe control valve, and the pipe control valve,
Wherein,
The water supply amount measured by the measuring means for measuring the water supply amount stored in the water supply tank storing the water supply water heated by the low-pressure water supply heater and the number of times stored in the hot well of the water supply heater, Wherein the control means controls the opening degree of one of the branch pipe control valve, the multiple pipe control valve and the weight control valve, or interlocks the two or more valve opening means simultaneously or at a time difference,
Wherein the controller is responsive to a decrease in the output of the generator and for determining a valve position of the branch control valve, a signal for determining a valve position of the plurality of pipe control valves, Wherein the control means controls the opening of the branch control valve, the plurality of pipe control valves, and the throttle control valve in accordance with the output compensation request signal including the signal.
delete

Images