CN107780986B

CN107780986B - Pump system, operating method thereof and power generation equipment

Info

Publication number: CN107780986B
Application number: CN201710598324.3A
Authority: CN
Inventors: 渡边将之; 山口学; 田岛卡洛斯; 花井豪; 今治义典
Original assignee: Mitsubishi Hitachi Power Systems Ltd
Current assignee: Mitsubishi Power Ltd
Priority date: 2016-08-26
Filing date: 2017-07-18
Publication date: 2020-04-21
Anticipated expiration: 2037-07-18
Also published as: JP2018031328A; CN107780986A; CN110953027A; CN110953027B; JP6771338B2

Abstract

A pump system capable of appropriately managing a flow rate is provided. Comprising: a fluid line for flowing a fluid; a pressure loss device provided in the fluid line; at least one booster pump which is provided on the downstream side of the pressure loss device of the fluid line and which is configured to boost the pressure of the fluid so as to compensate for at least a part of the pressure loss device; a bypass line that branches from the fluid line on an upstream side of the pressure loss device of the fluid line and merges with the fluid line on a downstream side of the booster pump; a bypass valve provided in the bypass line and configured to be opened and closed by a manual operation or a drive source; and a check valve which is provided in series with the bypass valve in the bypass line and is opened and closed by a front-rear differential pressure.

Description

Pump system, operating method thereof and power generation equipment

Technical Field

The invention relates to a pump system, a method for operating the same, and a power generation device.

Background

For example, in a condensate system facility of a power plant such as thermal power or nuclear power, in order to improve the quality of water supplied to a boiler or a steam generator, a facility (hereinafter, referred to as a pressure loss facility) is provided which includes an iron removal device, a desalination device, and the like and generates a pressure loss of condensate when the condensate passes through these devices. Further, a booster pump may be provided to compensate for the pressure loss of the pressure loss device.

Patent document 1 discloses a pump system in which an iron removal device is provided in series with a booster pump, and a bypass line is provided to bypass the iron removal device and the booster pump, in relation to a condensate water system facility of a power generation facility.

In this configuration, when the iron removing device is not used, the bypass valve provided in the bypass line can be fully opened to feed water through the bypass line, and the iron removing device can be repaired or inspected during operation of the facility.

Patent document 1: japanese unexamined patent publication No. 2001-296061

In the configuration described in patent document 1, when the booster pump fails, for example, the bypass valve is fully opened manually or by a drive source, and the usage flow path needs to be switched to the bypass line. In this case, during the operation of the bypass valve to the bypass valve before full opening, the flow rate of the system fluctuates, and therefore, the operation of the equipment may be affected.

In addition, when the bypass valve is erroneously opened for some reason during the operation of the pressure loss device and the booster pump, the fluid boosted in pressure by the booster pump flows back to the bypass line, and thus an excessive flow state may occur in which the flow rate of the booster pump exceeds the rated flow rate. When an over-flow state of the booster pump occurs, damage due to cavitation may occur to the equipment on the downstream side of the booster pump, and the operation of the equipment may be affected.

Disclosure of Invention

In view of the above conventional problems, an object of the present invention is to provide a pump system, an operating method thereof, and a power generation facility, which can appropriately manage a flow rate.

(1) A pump system according to at least one embodiment of the present invention includes: a fluid line for flowing a fluid; a pressure loss device provided in the fluid line; at least one booster pump configured to be provided on a downstream side of the pressure loss device in the fluid line, and to boost pressure of the fluid so as to compensate for at least a part of a pressure loss of the pressure loss device; a bypass line that branches from the fluid line on an upstream side of the pressure loss device in the fluid line and merges with the fluid line on a downstream side of the booster pump; a bypass valve provided in the bypass line and configured to be opened and closed manually or by a drive source; and a check valve that is provided in the bypass line in series with the bypass valve and is opened and closed by a front-rear differential pressure.

In the pump system described in (1) above, the bypass valve is always in the open state regardless of the operating state of the booster pump, and the check valve that is opened and closed by the front-rear differential pressure can be maintained in the closed state by the pressure of the fluid that is boosted by the booster pump during operation of the booster pump. Further, when the booster pump is tripped (operation is stopped due to a failure or the like), the check valve is quickly switched to the open state by a change in the differential pressure between the front and rear sides because the fluid of the booster pump is not boosted.

Therefore, the burden of the operation of the work operator can be reduced as compared with the case where the two lines are switched by manually opening and closing the bypass valve. Further, since the check valve can be quickly closed by the differential pressure between the front and rear of the check valve, the flow rate can be appropriately controlled while suppressing the flow rate fluctuation.

Further, since the opening and closing operation of the bypass valve is not required when the fluid line and the bypass line are switched, the operation error of the bypass valve by the operator does not occur. Therefore, the pump system and the device using the pump system can be improved in reliability, and the occurrence of backflow to the bypass line due to an overflow state of the booster pump can be suppressed by the check valve, and the flow rate can be appropriately controlled.

(2) In some embodiments, in the pump system described in (1) above, the check valve is provided downstream of the bypass valve in the bypass line.

In the pump system according to the above (2), compared to the case where the check valve is provided on the upstream side of the bypass valve in the bypass line, the flow path cross-sectional area of the bypass valve and the like are not directly affected by the pressure on the downstream side of the check valve (the pressure of the fluid boosted by the booster pump), and therefore the reliability of the opening and closing operation of the check valve can be improved.

(3) In some embodiments, in the pump system according to (1) or (2), the pressure loss device is a condensate demineralizer that demineralizes condensate condensed by a condenser.

In the pump system according to the above (3), in the pump system provided with the booster pump for compensating for at least a part of the pressure loss generated in the condensate demineralizer, the flow rate can be appropriately controlled as described in the above (1).

(4) In some embodiments, in the pump system according to any one of (1) to (3), the fluid line includes a plurality of flow paths arranged in parallel on a downstream side of the pressure loss device, and the at least one booster pump includes a plurality of booster pumps provided in the plurality of flow paths, respectively.

In the pump system according to the above (4), even when one or two or more booster pumps are stopped due to a failure or the like, the check valve is opened by the front-rear differential pressure, and the line to be used is quickly switched to the bypass line, so that the fluctuation of the flow rate can be suppressed, and the influence on the operation of the equipment can be reduced.

(5) A pump system according to at least one embodiment of the present invention includes: a plurality of flow paths arranged in parallel for flowing a fluid; a plurality of booster pumps provided in the plurality of flow paths, respectively; and a control device configured to suppress occurrence of an excessive flow state in which a flow rate of one booster pump exceeds a rated flow rate due to independent operation of the one booster pump among the plurality of booster pumps.

In the pump system according to the above (5), by suppressing the occurrence of an excessive flow state of one booster pump due to the independent operation of the booster pump by the control device, it is possible to suppress damage to the equipment on the downstream side of the booster pump due to cavitation.

(6) In some embodiments, in the pump system according to (5), the control device is configured to control the plurality of booster pumps such that one of the plurality of booster pumps is not operated alone in at least a high load zone in a device in which the pump system is installed.

In the pump system according to the above (6), since the separate operation of the booster pump can be avoided in a high load zone in which an excessive flow state of the booster pump is likely to occur, damage to the equipment due to cavitation can be effectively suppressed.

(7) In some embodiments, in the pump system according to (6), the control device includes a total operation control unit that starts or stops the plurality of booster pumps together based on a total operation signal for starting or stopping the plurality of booster pumps together.

In the pump system according to the above (7), the master operation control unit simultaneously starts or stops the plurality of booster pumps together, whereby occurrence of an excessive flow rate state of the booster pumps can be suppressed, and the operation load of the work operator can be reduced.

(8) In some embodiments, in the pump system according to the above (6) or (7), the control device includes an individual operation prohibition control unit configured to prohibit an operation of individually starting or stopping the plurality of booster pumps in at least a high load zone of the equipment.

In the pump system according to the above (8), the occurrence of an excessive flow state of the booster pump due to an erroneous operation by the work operator can be suppressed by prohibiting the operation of starting or stopping the booster pump in the high load zone.

(9) In some embodiments, in the pump system according to any one of the above (5) to (8), the control device includes an automatic stop control unit configured to automatically stop the remaining booster pumps when one of the plurality of booster pumps stops in at least a high load zone of the equipment when the plurality of booster pumps are operated.

In the pump system according to the above (9), when one of the plurality of booster pumps is stopped, the occurrence of an excessive flow state of the remaining booster pumps can be suppressed, and the burden on the operator can be reduced.

(10) In some embodiments, in the pump system according to (9), the automatic stop control unit is configured to automatically stop the remaining booster pumps based on a trip signal indicating that one of the plurality of booster pumps trips.

In the pump system according to the above (10), when one of the plurality of booster pumps is stopped during operation, the remaining booster pumps can be quickly stopped based on the trip signal, so that occurrence of an excessive flow rate state of the remaining booster pumps can be suppressed, and the burden on the operator can be reduced.

(11) In some embodiments, in the pump system according to the above (9) or (10), the automatic stop control unit is configured to automatically stop the remaining booster pumps based on an emergency stop signal indicating that one of the plurality of booster pumps is to be brought into emergency stop by manual operation.

In the pump system according to the above (11), when one of the plurality of booster pumps is stopped during operation, the remaining booster pumps can be quickly stopped based on the emergency stop signal, so that occurrence of an overflow state of the remaining booster pumps can be suppressed, and a burden on an operator can be reduced.

(12) In some embodiments, in the pump system according to any one of the above (9) to (11), the automatic stop control unit is configured to automatically stop the remaining booster pumps based on a power supply voltage reduction signal indicating that a power supply voltage of one booster pump of the plurality of booster pumps is equal to or lower than a reference voltage.

In the pump system according to the above (12), when one of the plurality of booster pumps is stopped during operation, the remaining booster pumps can be quickly stopped based on the power supply voltage reduction signal, so that occurrence of an excessive flow rate state of the remaining booster pumps can be suppressed, and the burden on the operator can be reduced.

(13) In some embodiments, in the pump system according to any one of the above (9) to (12), the automatic stop control unit is configured to automatically stop the remaining booster pumps based on a pump stop signal indicating that one of the plurality of booster pumps is stopped.

In the pump system according to the above (13), when one of the plurality of booster pumps is stopped during operation, the remaining booster pumps can be quickly stopped based on the pump stop signal, so that occurrence of an excessive flow rate state of the remaining booster pumps can be suppressed, and the burden on the operator can be reduced.

(14) A power generation facility according to at least one embodiment of the present invention has the pump system according to any one of (1) to (13) above.

The power generation facility according to (14) above, which is provided with the pump system according to any one of (1) to (13) above, can appropriately control the flow rate of the pump system, and can stably operate the power generation facility.

(15) In an operation method of a pump system according to at least one embodiment of the present invention, the pump system includes: a fluid line for flowing a fluid; a pressure loss device provided in the fluid line; at least one booster pump configured to be provided on a downstream side of the pressure loss device in the fluid line, and to boost pressure of the fluid so as to compensate for at least a part of a pressure loss of the pressure loss device; a bypass line that branches from the fluid line on an upstream side of the pressure loss device in the fluid line and merges with the fluid line on a downstream side of the booster pump; a bypass valve provided in the bypass line; a check valve that is provided in the bypass line in series with the bypass valve and is opened and closed by a front-rear differential pressure; the operation method includes a pump operation step of operating the booster pump in a state where the bypass valve is opened.

In the method of operating a pump system according to item (15), the booster pump is operated in the pump operation step in a state in which the bypass valve is opened, and the check valve that is opened and closed by the differential pressure between the front and rear can be maintained in a closed state by using the pressure of the fluid that is boosted by the booster pump during operation of the booster pump. Further, when the booster pump stops operating due to a failure or the like, the check valve is switched to the open state due to a change in the front-rear differential pressure because the fluid is not pressurized by the booster pump.

Therefore, the burden on the operator can be reduced as compared with the case where the two lines are switched by manually opening and closing the bypass valve. Further, since the check valve can be quickly closed by the differential pressure between the front and rear of the check valve, the flow rate can be appropriately controlled while suppressing the flow rate fluctuation.

Further, since it is not necessary to perform the opening/closing switching operation of the bypass valve as described above, the erroneous operation of the bypass valve does not occur. Therefore, the pump system and the device using the pump system can be improved in reliability, and the occurrence of backflow to the bypass line due to an overflow state of the booster pump can be suppressed by the check valve, and the flow rate can be appropriately controlled.

(16) In some embodiments, the method of operating the pump system according to (15) above further includes a bypass valve full closing step of closing the bypass valve when the check valve leaks.

With the method for operating the pump system according to item (16), when leakage occurs in the check valve, the effect of suppressing backflow from the booster pump to the bypass line can be enhanced by closing the bypass valve, and the flow rate can be appropriately managed by effectively suppressing the occurrence of an excessive flow rate state in the booster pump.

(17) In an operation method of a pump system according to at least one embodiment of the present invention, the pump system includes: a plurality of flow paths arranged in parallel for flowing a fluid; a plurality of booster pumps provided in the plurality of flow paths, respectively; the operation method includes an excess flow rate suppressing step of suppressing occurrence of an excess flow rate state in which a flow rate of one booster pump exceeds a rated flow rate due to independent operation of the one booster pump among the plurality of booster pumps.

In the pump system according to the above (17), the generation of an excessive flow state of one booster pump due to the independent operation of the booster pump is suppressed by the excessive flow suppressing step, and damage to the equipment on the downstream side of the booster pump due to cavitation can be suppressed.

ADVANTAGEOUS EFFECTS OF INVENTION

At least one embodiment of the present invention provides a pump system capable of appropriately managing a flow rate, a method of operating the pump system, and a power generation facility.

Drawings

Fig. 1 is a schematic diagram of a nuclear power plant 100 according to an embodiment of the present invention.

Fig. 2 is a diagram for explaining the use timing of the desalination device during the period from the start-up time to the stop time of the atomic power plant 100.

Fig. 3 is a diagram showing a detailed configuration of the pumping system 16 according to an embodiment, and shows an open/close state of each valve in a case where the condensate demineralization apparatus 30 is not used (during normal operation of the nuclear power plant 100, etc.).

Fig. 4 is a diagram showing a detailed configuration of the pumping system 16 according to an embodiment, and shows an open/close state of each valve in a case where the condensate demineralization apparatus 30 is used (at the time of start-up, at the time of stop, at the time of deterioration of water quality due to seawater leakage, and the like of the nuclear power plant 100).

Fig. 5 is a diagram showing a detailed configuration of a pump system 016 of a comparative system in which no check valve is provided, and shows an open/close state of each valve in a case where the condensate demineralizer 30 is not used (during normal operation of the nuclear power plant 100, etc.).

Fig. 6 is a diagram showing a detailed configuration of a pump system 016 of a comparative system in which no check valve is provided, and shows an open/close state of each valve in a case where the condensate demineralizer 30 is used (at the time of start-up, at the time of stop, at the time of deterioration of water quality due to seawater leakage, and the like of the nuclear power plant 100).

Fig. 7 is a diagram showing a state in which one condensate booster pump 32 of the plurality of condensate booster pumps 32 is tripped.

Fig. 8 is a diagram showing a state in which two condensate booster pumps 32 out of the plurality of condensate booster pumps 32 are tripped.

Fig. 9 is a diagram showing a detailed structure of pump system 16 according to an embodiment.

Fig. 10 is a diagram showing an example of the work order of the work operator and the control flow of the control device 46 according to the embodiment.

Fig. 11 is a diagram showing an example of a screen of the touch panel 48 according to the embodiment.

Fig. 12 is a diagram showing an example of a control flow of the control device 46 according to the embodiment.

Fig. 13 is a diagram showing an example of the overall operation control flow of the overall operation control unit 52.

Fig. 14 is a diagram showing an example of a screen of the overall control flow of the touch panel 48.

Fig. 15 is a diagram showing an example of the erroneous operation prevention control flow of each operation prohibition control unit 54.

Fig. 16 is a diagram showing an example of a screen of the erroneous operation prevention flow of the touch panel 48.

Fig. 17 is a diagram showing an example of a chain control flow of the automatic stop control unit.

Description of the reference numerals

2 steam generator

4 high-pressure turbine

6 moisture separation heater

8 low-pressure turbine

10 condenser

12 condensed water pump

14 gland steam condenser

16 pumping system

18 valve

20 low pressure water supply heater

22 degasser

24 water supply pump

26 high-pressure water supply heater

28 condensate desalination circuit

30 condensate demineralizer

32 condensed water booster pump

34 bypass line

36 bypass valve

38 check valve

40 flow path

42 desalter inlet valve

44 pump outlet valve

46 control device

48 touch screen

49 vapor pressure sensor

50 input interface

52 general operation control part

54 respectively operate the inhibition control parts

56 automatic stop control part

58 output interface

60 air exhaust pipe

62 discharge pipe

100 device

100 atomic force device

Mp1, Mp2 general instruction menu

Mp3 general instruction menu

Mp4, Mp5 define instruction menus

P1, P2, V1, V2 icons

Detailed Description

Hereinafter, several embodiments of the present invention will be described with reference to the drawings. The dimensions, materials, shapes, relative arrangements, and the like of the constituent members described as the embodiments and shown in the drawings are not intended to limit the scope of the present invention, and are merely illustrative examples.

For example, the terms "in a certain direction", "along a certain direction", "parallel", "orthogonal", "central", "concentric" or "coaxial" and the like are used in terms of relative or absolute arrangement, and do not strictly indicate the arrangement, but indicate a state of relative displacement with a tolerance, an angle to the extent that the same function can be obtained, or a distance.

For example, terms such as "identical", "equal", and "uniform" indicate that objects are identical, do not strictly indicate their arrangement, and indicate that there are tolerances or differences to the extent that the same function can be obtained.

For example, the term indicating the shape such as a square shape or a cylindrical shape does not indicate a shape such as a square shape or a cylindrical shape in a strict geometrical sense, but indicates a shape including a concave and convex portion or a rounded portion within a range where the same effect can be obtained.

On the other hand, the terms "having", "including", "containing" or "existing" do not exclude other elements from being present.

Fig. 1 is a diagram showing a schematic configuration of a nuclear power plant 100 according to an embodiment of the present invention.

The atomic power generating equipment 100 shown in fig. 1 includes: a steam generator 2, a high pressure turbine 4, a moisture separation heater 6, a low pressure turbine 8, a condenser 10, a plurality of condensate pumps 12, a gland steam condenser 14, a pumping system 16, a valve 18, a low pressure feed water heater 20, a deaerator 22, a plurality of feed water pumps 24, and a high pressure feed water heater 26.

The steam generator 2 generates steam by using heat from a not-shown atomic furnace. The steam generated by the steam generator 2 drives the high-pressure turbine 4 and the low-pressure turbine 8 sequentially through the high-pressure turbine 4, the moisture separation heater 6, and the low-pressure turbine 8. The high-pressure turbine 4 and the low-pressure turbine 8 are coupled to an unillustrated generator, and the generator generates electric power as the high-pressure turbine 4 and the low-pressure turbine 8 rotate.

The steam passing through the low-pressure turbine 8 is condensed by heat exchange with seawater by the condenser 10, and is temporarily stored in the condenser 10. The condensed water temporarily stored in the condenser 10 is pressurized by a plurality of condensed water pumps 12 arranged in parallel, and supplied to a pumping system 16 through a gland steam condenser 14.

Pump system 16 includes a condensate demineralization circuit 28 (fluid circuit), a condensate demineralizer 30 (pressure loss device), a plurality of condensate-assisted pumps 32, a bypass circuit 34, a bypass valve 36, and a check valve 38.

The condensate demineralizer 30 is provided in the condensate demineralization line 28, and demineralizes condensate (condensate) condensed by the condenser 10. In the condensate demineralization apparatus 30, demineralization of condensate is performed using, for example, an ion exchange resin.

The condensate demineralization line 28 includes a plurality of flow paths 40 arranged in parallel on the downstream side of the condensate demineralization apparatus 30, and the plurality of condensate booster pumps 32 are provided in the plurality of flow paths 40, respectively. In the illustrated exemplary embodiment, two condensate booster pumps 32 are provided in two flow paths 40 arranged in parallel, respectively.

The plurality of condensate booster pumps 32 are configured to boost the condensate pressure to compensate for at least a portion of the pressure loss of the condensate demineralizer 30.

The bypass line 34 is configured to branch from the condensate demineralization line 28 on the upstream side of the condensate demineralization apparatus 30 of the condensate demineralization line 28, and to merge with the condensate demineralization line 28 on the downstream side of the condensate booster pump 32. That is, the bypass line 34 is configured to bypass the condensate demineralizer 30 and the condensate booster pump 32.

The bypass valve 36 is provided in the bypass line 34, and can be opened and closed at any timing by a drive source such as a manual or motor even without a differential pressure between the front and rear of the bypass valve 36.

The check valve 38 is provided in series with the bypass valve 36 on the downstream side of the bypass valve 36 in the bypass line 34, and is opened and closed by a front-rear differential pressure (a differential pressure between the upstream side and the downstream side of a valve element, not shown, of the check valve 38). Specifically, the check valve 38 allows only the forward flow from the upstream side (the condenser 10 side in the flow direction of the condensed water) to the downstream side (the low-pressure feed water heater 20 side in the flow direction of the condensed water) of the check valve 38, and does not allow the reverse flow.

The condensed water passing through the pumping system 16 is heated by the low-pressure feed water heater 20 through the valve 18, and then flows into the deaerator 22. The condensed water heated and deaerated in the deaerator 22 is pressurized by a plurality of feed pumps 24 provided in parallel, heated by a high-pressure feed water heater 26, and then fed to the steam generator 2.

Here, the use timing of the condensate demineralizer 30 during the period from the start-up time to the stop time of the nuclear power plant 100 will be described with reference to fig. 1 and 2.

As shown in fig. 2, when the nuclear power plant 100 is started, stopped, or when the water quality deteriorates due to seawater leakage, the condensate demineralizer 30 is used to improve the water quality without using the bypass line 34. On the other hand, during normal operation of the nuclear power plant 100 (except when the water quality deteriorates), the bypass line 34 is used without using the condensate demineralization apparatus 30. Since the pump system 16 shown in fig. 1 includes two condensate booster pumps 32 of the same configuration arranged in parallel, both of the two condensate booster pumps 32 are operated so that an excessive flow rate state in which the flow rate exceeds the rated flow rate does not occur in the condensate booster pumps 32 in a high load zone (see fig. 2) in which the load of the nuclear power plant 100 is 50% or more.

The reason why the condensate demineralization apparatus 30 is used at the time of starting and stopping the nuclear power plant 100 is that, in general, there is water that flows into the condenser through a system in which water is not passed for a long period of time at the time of starting and stopping the power plant. Therefore, as described above, the condensate demineralization apparatus 30 is used to improve the water quality at the time of starting, stopping, and deteriorating the water quality due to seawater leakage of the nuclear power plant 100.

Fig. 3 and 4 show an example of a detailed configuration of the pump system 16. Fig. 3 shows the open/close state of each valve in the case where the condensate demineralizer 30 is not used (during normal operation of the nuclear power plant 100, etc.), and fig. 4 shows the open/close state of each valve in the case where the condensate demineralizer 30 is used (during startup, shutdown, and deterioration in water quality due to seawater leakage, etc.) in the nuclear power plant 100. In fig. 3 and 4, the two triangular marks including the blank space indicate the valve in the open state, and the two triangular marks including the black space indicate the valve in the closed state. In the embodiment shown in fig. 3 and 4, a desalination device inlet valve 42 is provided upstream of the condensate demineralization device 30 in the condensate demineralization line 28, and a plurality of pump outlet valves 44 are provided downstream of the plurality of condensate booster pumps 32 in the plurality of flow paths 40, respectively.

As shown in fig. 3, during normal operation of the nuclear power plant 100, the condensate booster pump 32 is stopped and the pump outlet valve 44 is closed because the bypass line 34 is used instead of the condensate demineralization line 28. The desalter inlet valve 42 and the bypass valve 36 are opened regardless of the presence or absence of use of the condensate demineralizer 30. Since there is no pressure difference between the downstream side and the upstream side of the check valve 38 while the condensate booster pump 32 is stopped, the check valve 38 is maintained in the open state by the flow of the condensate water. Therefore, during the stop of the condensate booster pump 32, the entire amount of the condensate supplied from the condenser 10 to the pumping system 16 is supplied to the low-pressure feed water heater 20 through the bypass line 34.

On the other hand, as shown in fig. 4, at the time of starting, stopping, and deterioration of water quality due to seawater leakage of the nuclear power plant 100, the condensate demineralization line 28 is used to improve the water quality without using the bypass line 34, and therefore the condensate booster pump 32 is driven and the pump outlet valve 44 is fully opened. During operation of the condensate booster pump 32, the condensate is boosted by the condensate booster pump 32 so that the pressure on the downstream side of the check valve 38 becomes sufficiently higher than the pressure on the upstream side of the check valve 38, and therefore the check valve 38 can be maintained in a closed state by the front-rear differential pressure of the check valve 38. Therefore, in operation of the condensate booster pump 32, all of the amount of condensate supplied from the condenser 10 to the pumping system 16 is supplied to the low pressure feedwater heater 20 through the condensate desalination line 28.

With the pump system 16 shown in fig. 3 and 4, the bypass valve 36 is always opened regardless of the operating state of the condensate booster pump 32, and the check valve 38 that is opened and closed by a front-rear differential pressure can be maintained in a closed state by the pressure of the fluid that is boosted by the condensate booster pump 32 during the operation of the condensate booster pump 32. When the operation of the condensate booster pump 32 is stopped, the pressure of the fluid in the condensate booster pump 32 is not increased, and there is no differential pressure between the front and rear of the check valve 38, so that the check valve 38 is switched to the open state.

Therefore, the burden on the operator can be reduced compared to the case where the check valve 38 is not provided (the case where the two

lines

28 and 34 are switched by opening and closing the bypass valve 36 by a manual or driving source as shown in fig. 5 and 6). Further, since the check valve 38 can be quickly closed by the differential pressure between the front and rear of the check valve 38, the flow rate can be appropriately controlled by suppressing the flow rate fluctuation when the two

lines

28 and 34 are switched.

For example, as shown in fig. 7, when one condensate booster pump 32 of the plurality of condensate booster pumps 32 is tripped, if the remaining condensate booster pumps 32 are quickly stopped, the check valve 38 closed by the discharge pressure of the condensate booster pump 32 is opened, whereby the use line can be quickly switched to the bypass line 34, and the fluctuation in the flow rate of condensate water can be suppressed. Further, as shown in fig. 8, even when all of the plurality of condensate booster pumps 32 are tripped at the same time, the check valve 38 closed by the discharge pressure of the condensate booster pumps 32 is opened, whereby the use line can be quickly switched to the bypass line 34, and the fluctuation in the flow rate of the condensate water can be suppressed. Therefore, the nuclear power plant 100 can be stably operated.

Further, since the opening and closing operation of the bypass valve 36 is not required at the time of switching between the condensate demineralization circuit and the bypass circuit 34, the operation of the bypass valve 36 by the operator is not erroneously performed. Therefore, the pump system 16 and the nuclear power plant 100 using the same can be improved in reliability, and the check valve 38 can suppress the occurrence of backflow to the bypass line 34 due to the excessive flow rate state of the condensate booster pump 32, thereby appropriately managing the flow rate.

In one embodiment, the bypass valve 36 may be closed when the check valve 38 leaks. This can suppress the backflow from the condensate booster pump 32 to the bypass line 34, and can suppress the occurrence of an excessive flow rate state of the condensate booster pump 32.

In one embodiment, as shown in fig. 9, pump system 16 may also have: a control device 46 configured to control the condensate booster pump 32; a touch panel 48 (operation unit) for the worker to operate the condensate booster pump 32; a vapor pressure sensor 49 for measuring an inlet vapor pressure of the low-pressure turbine 8 (see fig. 1). The illustrated control device 46 includes: the input interface 50, the overall operation control unit 52, the operation prohibition control unit 54, the automatic stop control unit 56, and the output interface 58, respectively.

Fig. 10 is a diagram showing an example of the work order of the work operator and the control flow of the control device 46 according to the embodiment. Fig. 11 is a diagram showing an example of a screen of the touch panel 48 according to the embodiment.

As shown in fig. 11, icons P1, P2 corresponding to the respective condensate booster pumps 32 of the pump system 16 and icons V1, V2 corresponding to the respective pump outlet valves 44 are displayed on the touch panel 48.

As shown in fig. 10, first, in S11, the work operator determines the operation condition of the atomic power generating equipment 100. Specifically, it is determined whether the water quality is deteriorated, or not, corresponding to the start-up of the nuclear power plant 100, the stop of the plant, or the like.

When it is determined at S11 that the operation corresponds to either the start, stop, or deterioration of the water quality of the nuclear power plant 100, at S12, the operator touches the icons P1 and P2 on the touch panel 48 shown in fig. 11, and selects "on" from the normal command menus Mp1 and Mp2 displayed in association with the respective icons. Accordingly, in S13, the controller 46 starts each condensate booster pump 32, and in S14, the controller 46 fully opens each pump outlet valve 44.

When the work operator determines that the atomic power plant 100 is operating normally in S11, the work operator touches the icons P1 and P2 of the touch panel 48 shown in fig. 11 in S15 to select "off" from the normal command menus Mp1 and Mp2 displayed in association with the respective icons. Accordingly, the controller 46 completely closes each pump outlet valve 44 in S16, and the controller 46 stops each condensate booster pump 32 in S17.

Fig. 12 is a diagram illustrating an example of a control flow of the control device 46 according to the embodiment. The control device 46 is configured to suppress the occurrence of an excessive flow state in which the flow rate of one of the condensate booster pumps 32 exceeds the rated flow rate due to the independent operation of the one of the condensate booster pumps 32. As described below, the controller 46 performs the total operation control by the total operation controller 52 in S21, performs the erroneous operation prevention control by the individual operation prohibition controller 54 in S22, and performs the interlock control by the automatic stop controller 56 in S23. The order of the respective controls is not particularly limited, and the respective controls from S21 to S23 can be independently performed. The following describes the contents of the respective controls.

Fig. 13 is a diagram showing an example of the overall operation control flow of the overall operation control unit 52. Fig. 14 is a diagram showing an example of a screen of the overall control flow of the touch panel 48.

As shown in fig. 13, first, in S31, it is determined whether or not the "all" button on the screen shown in fig. 14 has been pressed.

When the all button is pressed in S31, it is determined in S32 whether or not the all button in the total command menu Mp3 on the screen shown in fig. 14 is pressed. In one embodiment, when the "full on" button is pressed, a total operation signal for simultaneously starting the plurality of condensate booster pumps 32 is input from the touch panel 48 to the input interface 50 of the control device 46, and it is determined that the "full on" button is pressed based on the total operation signal. On the other hand, when the "full stop" button is pressed, a total operation signal for simultaneously stopping the plurality of condensate booster pumps 32 is input from the touch panel 48 to the input interface 50 of the control device 46, and it is determined that the "full stop" button is pressed based on the total operation signal.

If it is determined at S32 that the "full-on" button has been pressed, the overall operation control unit 52 simultaneously activates the plurality of condensate booster pumps 32 via the output interface 58 at S33, and simultaneously fully opens the plurality of pump outlet valves 44 at S34.

If it is determined at S31 that the all button has not been pressed, the operation returns to the start. If it is determined in S32 that the "full on" button has not been pressed (the "full off" button has been pressed), the overall operation control unit 52 fully closes the plurality of pump outlet valves 44 all at once via the output interface 58 in S35, and stops the plurality of condensate booster pumps 32 all at once in S36.

In this way, the master operation control unit 52 can simultaneously start or stop the plurality of condensate booster pumps 32 together, thereby suppressing the occurrence of an excessive flow state in which the flow rate of one of the plurality of condensate booster pumps 32 exceeds the rated flow rate due to the operation of the one condensate booster pump 32 alone. Further, the burden on the operator can be reduced as compared with the case where the condensate booster pumps 32 are individually started or stopped.

Fig. 15 is a diagram showing an example of the erroneous operation prevention control flow of each operation prohibition control unit 54. Fig. 16 is a diagram showing an example of a screen of the erroneous operation prevention flow of the touch panel 48.

As shown in fig. 15, first, it is determined at S41 whether or not the atomic power generating equipment 100 is operating in the high load zone. When it is determined at S41 that the nuclear power plant 100 is operating in the high load zone, at S42 the individual operation prohibition control unit 54 invalidates, i.e., prohibits, the operation of individually starting or stopping the plurality of condensate booster pumps 32. In S43, when the worker operates the icon P1 or P2 on the screen of the touch panel 48 shown in fig. 16, the condensed water assist pump 32 corresponding to the icon P1 or P2 displays the restriction instruction menu Mp4 or Mp 5. In the limit command menus Mp4 and Mp5, the "on" button for activating each of the condensate booster pumps 32, the "off" button for stopping each of the condensate booster pumps 32, and the "off" button, which is an emergency stop button of each of the condensate booster pumps 32, cannot be operated, and only the "off-hook" button can be operated.

When it is determined at S41 that the nuclear power plant 100 is not operating in the high load zone, at S44 the individual operation prohibition control unit 54 validates the operation of starting or stopping the individual condensate booster pumps 32. In S45, when the worker operates the icon P1 or P2 on the screen of the touch panel 48 shown in fig. 16, the normal instruction menu Mp1 or Mp2 (see fig. 14) is displayed for the condensate booster pump 32 corresponding to the icon P1 or P2. The general command menus Mp1, Mp2 enable all operations of the above-described "on" button, "off" button, and "off-hook" button.

In this way, the operation of individually activating or deactivating the respective condensate booster pumps 32 is inhibited at least in the high load zone by the individual operation inhibition control unit 54, and the occurrence of the excessive flow rate state of the condensate booster pumps 32 due to the erroneous operation by the operator can be suppressed. In the control flow, the limiting command menus Mp4 and Mp5 are displayed in a manner that the condensate booster pumps 32 cannot be started or stopped in the high load zone of the nuclear power plant 100, and the normal command menus Mp1 and Mp2 may be displayed in the high load zone of the nuclear power plant 100, and the signals of the operation are not received even when the buttons for operating the respective condensate booster pumps 32 are pressed.

Fig. 17 is a diagram illustrating an example of an interlock control flow of the automatic stop control unit 56.

As shown in fig. 17, first, at S51, it is determined whether or not the atomic power plant 100 is operating in the high load zone. When it is determined at S51 that the nuclear power plant 100 is operating in the high load zone, it is determined at S52 whether or not a trip signal indicating that one condensate booster pump 32 of the plurality of condensate booster pumps 32 is determined to be tripped is received from the condensate booster pump 32. If it is determined at S52 that the trip signal has been received, at S56, the automatic stop control unit 56 automatically stops the remaining condensate booster pumps 32.

If it is not determined in S52 that the trip signal has been received, it is determined in S53 whether an emergency stop signal indicating that one condensate booster pump 32 of the plurality of condensate booster pumps 32 has been manually stopped has been received from the touch panel 48. If it is determined at S53 that the emergency stop signal has been received, the automatic stop control unit 56 automatically stops the remaining condensate booster pumps 32 at S56.

If it is not determined at S53 that the emergency stop signal has been received, it is determined at S54 whether or not a power supply voltage drop signal indicating that the power supply voltage (bus voltage) of one condensate booster pump 32 of the plurality of condensate booster pumps 32 is equal to or less than the reference voltage has been received from the condensate booster pump 32. If it is determined at S54 that the power supply voltage reduction signal has been received, the automatic stop control unit 56 automatically stops the remaining condensate booster pumps 32 at S56.

If it is not determined in S54 that the power supply voltage reduction signal has been received, it is determined in S55 whether a pump stop signal indicating that one condensate booster pump 32 of the plurality of condensate booster pumps 32 has been stopped for some reason has been received from the condensate booster pump 32. When it is determined at S55 that the pump stop signal has been received, the automatic stop control unit 56 automatically stops the remaining condensate booster pumps 32 at S56.

The pump stop signal may be transmitted from a tachometer to the control device 46, for example, when the rotational speed of the condensate booster pump 32 is monitored by a tachometer, not shown, and the rotational speed measured by the tachometer is equal to or less than a reference value.

In one embodiment, when a threshold value (allowable time) is set at the detection time of the pump stop signal and the pump stop signal is continuously received for a time longer than the threshold value in S54, the automatic stop control unit 56 may automatically stop the remaining condensed water assist pump 32 in S56. In this case, the threshold value may be determined in consideration of the pump design requirement value.

At S57, the remaining condensate booster pumps (residual machines) 32 of the plurality of condensate booster pumps 32 issue an alarm indicating that an automatic stop command has been issued.

In this way, when one of the plurality of condensate booster pumps 32 is stopped during operation, by performing the interlock control of automatically stopping the remaining condensate booster pumps 32 by the automatic stop control unit 56, it is possible to suppress the occurrence of the excessive flow rate state of the remaining condensate booster pumps 32 and to reduce the burden on the operator.

Further, since the determinations shown in S52 to S54 are performed before it is determined whether or not the pump stop signal indicating the actual stop of the condensate booster pump 32 is received in S55, the remaining condensate booster pumps 32 can be automatically stopped faster than the actual stop of the condensate booster pump 32, and the occurrence of the excessive flow rate state can be effectively suppressed.

In S41 and S51, for example, when the inlet steam pressure of the low-pressure turbine 8 measured by the steam pressure sensor 49 (see fig. 9) is higher than a threshold value, it may be determined that the nuclear power plant 100 is operating in the high load band, and when the inlet steam pressure is lower than the threshold value, it may be determined that the nuclear power plant 100 is operating in the low load band.

Further, at the time of starting the nuclear power plant 100, since the flow rate of the condensate water is increased by the discharge collected into the condenser 10 as compared with the normal operation, even at the time of starting the nuclear power plant 100 in which the flow rate of the condensate water is increased, when the threshold value of the inlet vapor pressure is set so that the generation of the excessive flow rate of the condensate water booster pump 32 can be avoided, the generation of the excessive flow rate of the condensate water booster pump 32 can be avoided from the time of starting to the time of stopping the nuclear power plant 100. For example, in the pump system 16, the pressure level corresponding to 20% to 40% of the load output by the turbine may be set as the threshold value.

The present invention is not limited to the above embodiments, and may include modifications of the above embodiments, and combinations of these embodiments as appropriate.

For example, in the above embodiment, the pump system 16 has been described by taking the nuclear power plant 100 as an example, and the pump system 16 is not limited to the nuclear power plant, and can be applied to a thermal power plant, a plant, or the like.

Claims

1. A pump system, comprising:

a fluid line for flowing a fluid;

a pressure loss machine provided in the fluid line;

at least one booster pump provided on a downstream side of the pressure loss device in the fluid line, and configured to boost pressure of the fluid so as to compensate for at least a part of a pressure loss of the pressure loss device;

a bypass line that branches from the fluid line on an upstream side of the pressure loss device in the fluid line and merges with the fluid line on a downstream side of the booster pump;

a bypass valve provided in the bypass line and configured to be opened and closed manually or by a drive source;

a check valve that is provided in the bypass line in series with the bypass valve and is opened and closed by a front-rear differential pressure;

the fluid line includes a plurality of flow paths arranged in parallel on a downstream side of the pressure loss machine,

the at least one booster pump includes a plurality of booster pumps provided in the plurality of flow paths, respectively,

the fluid line is configured to merge fluids passing through the plurality of booster pumps.

2. The pump system of claim 1,

the check valve is provided on a downstream side of the bypass valve of the bypass line.

3. The pump system of claim 1,

the pressure loss machine is a condensate demineralizer for demineralizing condensate condensed by a condenser.

4. The pump system of claim 1,

the flow direction of the fluid line is a direction from the condenser to the feed water heater,

the flow direction of the fluid of the bypass line is a direction from the condenser to the feed water heater.

5. A power generation apparatus, characterized by having:

the pump system of any one of claims 1-4.

6. A method of operating a pump system, characterized in that,

the pump system has:

a fluid line for flowing a fluid;

a pressure loss machine provided in the fluid line;

a bypass valve provided in the bypass line;

the fluid line is configured to merge fluids passing through the plurality of booster pumps,

the operation method includes a pump operation step of operating the booster pump in a state where the bypass valve is opened.

7. Method for operating a pump system according to claim 6,

and a bypass valve full-closing step of closing the bypass valve when the check valve leaks.