WO2018066366A1 - Strainer cleaning device and method - Google Patents

Strainer cleaning device and method Download PDF

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Publication number
WO2018066366A1
WO2018066366A1 PCT/JP2017/034009 JP2017034009W WO2018066366A1 WO 2018066366 A1 WO2018066366 A1 WO 2018066366A1 JP 2017034009 W JP2017034009 W JP 2017034009W WO 2018066366 A1 WO2018066366 A1 WO 2018066366A1
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WO
WIPO (PCT)
Prior art keywords
line
valve
casing
drain
strainer
Prior art date
Application number
PCT/JP2017/034009
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French (fr)
Japanese (ja)
Inventor
大輝 藤村
Original Assignee
三菱日立パワーシステムズ株式会社
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Application filed by 三菱日立パワーシステムズ株式会社 filed Critical 三菱日立パワーシステムズ株式会社
Publication of WO2018066366A1 publication Critical patent/WO2018066366A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/02Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/16Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/48Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22DPREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
    • F22D11/00Feed-water supply not provided for in other main groups

Definitions

  • the present invention relates to an apparatus and method for cleaning a strainer provided in a water supply system of a power plant.
  • steam is generated by burning fuel in a boiler, transferring heat energy of the generated combustion gas to boiler feed water to generate steam, and rotating the steam turbine with the steam, thereby rotating the steam turbine.
  • the generator connected to the shaft is rotationally driven to generate electric power.
  • the steam that has been worked by rotating the steam turbine is condensed by heat exchange with cooling water and cooled by the condenser to be condensed water, and is returned to the boiler by the condensing water pump as water supply.
  • the present invention solves the above-mentioned problems, and an object of the present invention is to provide a strainer cleaning apparatus and method for shortening the cleaning processing time.
  • the inside of the casing is divided into an inlet side chamber and an outlet side chamber by a screen, and a water supply line is connected to the inlet side chamber to provide an inlet valve.
  • a water supply line is connected to the outlet side chamber and the outlet valve is provided, a backwash line connected to the outlet side chamber and capable of supplying washing water, a backwash valve provided on the backwash line, the inlet A differential pressure generating device for adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing, the drain line connected to the drain discharge side of the side chamber and capable of discharging foreign matter, the drain valve provided on the drain line And.
  • the differential pressure generator adjusts the pressure to be higher than the pressure on the drain discharge side of the casing
  • the treated water in the casing flows to the drain discharge side to lower the water level in the casing.
  • the backwash valve is opened to supply washing water from the backwash line to the outlet side chamber and the drain valve is opened, the foreign matter adhering to the strainer is removed, and the foreign matter is discharged from the inlet side chamber to the drain line Ru. That is, by adjusting the internal pressure of the casing to be higher than the pressure on the drain discharge side by the differential pressure generator, the treated water in the casing can be discharged at an early stage, and the processing time for cleaning the strainer is shortened. It can be improved.
  • the differential pressure generator includes a vent line connected to the outlet side chamber, a vent valve provided on the vent line, and a suction line connected to the drain discharge side of the outlet side chamber. And a suction valve provided in the suction line.
  • the water supply line is maintained at a vacuum pressure
  • the suction line is connected upstream of the inlet valve in the water supply line, and the internal pressure of the suction line It is characterized by raising the internal pressure.
  • the suction line is connected to the drain line, and a first drain valve and a first drain valve are provided as the drain valve upstream and downstream of a connection portion of the drain line with the suction line. 2) It is characterized in that a drain valve is provided.
  • the backwash valve is opened to supply wash water from the backwash line to the outlet side chamber, and the first drain valve and the second drain valve
  • the drain valve is opened, the foreign matter adhering to the strainer can be discharged from the inlet side chamber to the drain line, and the treated water remaining in the suction line can also be discharged.
  • the apparatus for cleaning a strainer according to the present invention is characterized in that a water level detection and estimation device for detecting or estimating the water level in the casing is provided.
  • the suction valve can be closed and the backwash valve and the drain valve can be opened to continuously carry out drainage and foreign matter removal in the casing.
  • a water level detection and estimation device for detecting or estimating the water level in the casing, and closing the suction valve when the water level in the casing falls to a predetermined water level set in advance
  • a valve and a control device for opening the drain valve are provided.
  • the suction valve is closed and the backwash valve and the drain valve are opened, so that drainage and foreign matter removal in the casing can be performed continuously.
  • the differential pressure generating device is characterized by having a pressure line connected to the inlet side chamber or the outlet side chamber, and a pressure valve provided to the pressure line.
  • the pressurizing valve when the pressurizing valve is opened, pressurizing force acts on the inlet side chamber from the pressurizing line, the internal pressure of the casing becomes higher than the pressure of the drain line, and the treated water in the casing can flow to the drain line.
  • the water level in the casing can be reduced early simply by connecting a pressure line to the inlet side chamber.
  • the pressurizing line is connected to a pressurizing device, and the internal pressure of the casing is made higher than the pressure of the drain line.
  • the treated water in the casing can be flowed to the drain line, and the water level in the casing can be reduced early.
  • the differential pressure generating device has a suction line connected to the pressure discharge device and the suction line connected to the drain side of the outlet side chamber, and suction provided to the suction line. And a valve, which is characterized in that the internal pressure of the casing is higher than the pressure of the suction line.
  • the water supply line is maintained at a vacuum pressure, and the suction line is connected upstream of the inlet valve in the water supply line.
  • the suction line is connected to the drain line, and a first drain valve and a first drain valve are provided as the drain valve upstream and downstream of a connection portion of the drain line with the suction line. 2) It is characterized in that a drain valve is provided.
  • the backwash valve is opened to supply wash water from the backwash line to the outlet side chamber, and the first drain valve and the second drain valve
  • the drain valve is opened, the foreign matter adhering to the strainer can be discharged from the inlet side chamber to the drain line, and the treated water remaining in the suction line can also be discharged.
  • the apparatus for cleaning a strainer according to the present invention is characterized in that a water level detection and estimation device for detecting or estimating the water level in the casing is provided.
  • the suction valve can be closed and the backwash valve and the drain valve can be opened to continuously carry out drainage and foreign matter removal in the casing.
  • a control device for closing the suction valve and opening the backwash valve and the drain valve when the water level in the casing falls to a predetermined water level set in advance. It is characterized.
  • the suction valve is closed and the backwash valve and the drain valve are opened, so that drainage and foreign matter removal in the casing can be performed continuously.
  • the inside of the casing is divided into an inlet side chamber and an outlet side chamber by a screen, and a water supply line is connected to the inlet side chamber to provide an inlet valve.
  • a water supply line is connected to the inlet side chamber to provide an inlet valve.
  • the internal pressure of the casing is adjusted to be higher than the pressure on the drain discharge side, so the treated water in the casing can be discharged early, thereby shortening the cleaning processing time of the strainer. can do.
  • FIG. 1 is a schematic view showing a cleaning device of a strainer according to a first embodiment.
  • FIG. 2 is a flowchart showing the method of cleaning the strainer according to the first embodiment.
  • FIG. 3 is a schematic view showing a thermal power plant.
  • FIG. 4 is a schematic view showing a cleaning device of a strainer according to a second embodiment.
  • FIG. 5 is a flowchart showing a method of cleaning a strainer according to a second embodiment.
  • FIG. 6 is a schematic view showing a strainer cleaning apparatus according to a third embodiment.
  • FIG. 7 is a flowchart showing a method of cleaning a strainer according to a third embodiment.
  • FIG. 3 is a schematic view showing a thermal power plant.
  • the thermal power plant burns fuel, generates steam with heat generated by combustion, and rotates a steam turbine with the produced steam to drive a generator connected to the steam turbine. It generates power.
  • the thermal power plant 10 includes a boiler 11, a steam turbine 12, a condenser 13, a strainer 14, a condensate pump 15, a low pressure feed water heater 16, and a deaerator 17. , A high pressure feed water heater 18 and a generator 19.
  • a conventional boiler is used for the boiler 11, and it is possible to burn pulverized coal as a fuel by a combustion burner and recover heat generated by this combustion using a furnace wall pipe 21 functioning as a heat transfer pipe .
  • the steam turbine 12 has a high pressure turbine 22, an intermediate pressure turbine 23, and a low pressure turbine 24.
  • the turbines 22, 23, 24 are integrally rotatably connected by a rotor 25 serving as a rotation shaft.
  • the main steam line 26 from the furnace wall pipe 21 of the boiler 11 is connected to the inflow side, and the low temperature reheat steam line 27 leading to the reheater (not shown) of the boiler 11 is connected to the outflow side. It is done.
  • the high pressure turbine 22 is rotated by the steam supplied from the main steam line 26 and discharges the used steam from the low temperature reheat steam line 27.
  • the high pressure reheat steam line 28 from the reheater of the boiler 11 is connected to the inflow side of the intermediate pressure turbine 23, and the steam line 29 leading to the low pressure turbine 24 is connected to the outflow side.
  • the medium pressure turbine 23 is rotated by the reheated steam supplied from the high temperature reheat steam line 28 and discharges the used steam from the steam line 29 toward the low pressure turbine 24.
  • the steam line 29 is connected to the low pressure turbine 24 at the inflow side, and the condenser 13 is connected to the outflow side.
  • the low pressure turbine 24 is rotated by the steam supplied from the steam line 29 and discharges the used steam to the condenser 13.
  • the generator 19 the rotations of the high pressure turbine 22, the intermediate pressure turbine 23, and the low pressure turbine 24 are transmitted through the rotor 25 and rotationally driven to generate electric power.
  • the condenser 13 condenses the steam discharged from the low pressure turbine 24 back to water (condensed water) by coming into contact with a cooling line through which the cooling water flows.
  • the condensed water generated by the condenser 13 is supplied to the low pressure feed water heater 16 by the condensate pump 15 after the foreign matter is removed by the strainer 14.
  • the first water supply line 31 connected to the outlet side of the condenser 13 is branched into two branch lines 32 and 33, collected again to form a second water supply line 34, and connected to the furnace wall pipe 21 of the boiler 11 ing.
  • the strainer 14 is composed of a first strainer 41 and a second strainer 42.
  • the first strainer 41 is provided in the branch line 32, the inlet valve 43 is provided on the inflow side, and the outlet valve 44 is provided on the outflow side.
  • the second strainer 42 is provided in the branch line 33, the inlet valve 45 is provided on the inflow side, and the outlet valve 46 is provided on the outflow side.
  • the inlet valve 43 and the outlet valve 44 of the first strainer 41 are shown as being white in the drawing, and the inlet valve 45 and the outlet valve 46 of the second strainer 42 are shown as being black. It shows. That is, the first strainer 41 is in the water flowing state, and the second strainer 42 is in the water blocking state.
  • the condensate pump 15, the low pressure feed water heater 16, the deaerator 17 and the high pressure feed water heater 18 are provided in series in the second branch line 34.
  • the low pressure feed water heater 16 heats the condensed water at a low pressure.
  • the heated water is supplied from the low pressure feed water heater 16 to the deaerator 17.
  • the deaerator 17 removes impurities such as dissolved oxygen and non-condensable gas (ammonia gas) from the condensed water supplied from the low pressure feed water heater 16.
  • Deaerated water is supplied from the deaerator 17 toward the high pressure feed water heater 18.
  • the high pressure feed water heater 18 heats the degassed condensate under high pressure.
  • the heated condensate is supplied from the high pressure feed water heater 18 toward the furnace wall pipe 21 of the boiler 11 as the feed water.
  • the condenser 13 cools the steam used in the steam turbine 12 with cooling water and condenses it for condensation to reduce the volume to create a high vacuum state and improve the flow of the steam to make the turbine Improve the efficiency of Therefore, the vacuum state is maintained at least the condenser 13, the strainer 14, and the first water supply line 31, the branch lines 32 and 33, and the second water supply line 34 to the condensate pump 15.
  • the water flowing in the furnace wall pipe 21 of the boiler 11 is heated by the internal flame to generate steam, and the generated steam is supplied to the steam turbine 12.
  • the steam supplied to the steam turbine 12 flows through the high pressure turbine 22, the intermediate pressure turbine 23, and the low pressure turbine 24 in order and flows into the condenser 13.
  • the steam turbine 12 is rotated by the flowed steam, so that the generator 19 is rotationally driven via the rotor 25, and the generator 19 generates electric power.
  • the steam flowing into the condenser 13 is returned to the condensate by being condensed by the cooling line.
  • the condensate condensed by the condenser 13 is subjected to the low pressure feed water heater 16, the deaerator 17 and the high pressure feed water heater 18 into the furnace wall pipe 21 of the boiler 11 after the foreign matter is removed by the strainer 14. Will be returned.
  • FIG. 1 is a schematic view showing a cleaning device of a strainer according to a first embodiment.
  • the screen (mesh) 52 is disposed in an inclined state in the casing 51 so that the inside of the first strainer 41 is divided into an inlet side chamber 53 and an outlet side chamber 54.
  • the inlet side chamber 53 is connected to the downstream end of the inlet line 32 a in the branch line 32, and the upstream end of the outlet line 32 b in the branch line 32 is connected to the outlet side chamber 54.
  • the inlet line 32 a is provided with an inlet valve 43
  • the outlet line 32 b is provided with an outlet valve 44.
  • a vent line 61 is connected to the outlet side chamber 54, and a vent valve 62 is provided in the vent line 61.
  • One end of the vent line 61 is open to the atmosphere, and the inside of the casing 51 is maintained in a sealed state by closing the vent valve 62, and the inside of the casing 51 is communicated to the atmosphere by opening the same.
  • the vent line 61 may be connected to the inlet side chamber 53 of the casing 51.
  • the backwash line 63 is connected to the outlet side chamber 54, and the backwash line 63 is provided with a backwash valve 64.
  • One end of the backwashing line 63 is connected to the second water supply line 34 (see FIG. 3), and by opening the backwashing valve 64, the water supply of the second water supply line 34 is used as cleaning water in the outlet side chamber 54. Can be supplied.
  • the drain line 65 is connected to the inlet side chamber 53, and the first drain valve 66 and the second drain valve 67 are provided in series in the drain line 65.
  • the drain line 65 is connected at one end to a waste water treatment facility (not shown), and the treated water and wash water in the inlet side chamber 53 can be discharged to the waste water treatment facility by opening the respective drain valves 66 and 67. it can.
  • the first strainer 41 is provided with a differential pressure generating device which adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65.
  • the differential pressure generator has a suction line 68 connected to the outlet side chamber 54 of the casing 51 and provided on the drain discharge side of the casing 51, and a vacuum valve (suction valve) 69 provided on the suction line 68. That is, one end of the suction line 68 is connected to the outlet side chamber 54 of the casing 51 and the other end is connected to the upstream side of the inlet valve 43 in the inlet line 32 a constituting the branch line 32.
  • the suction line 68 is connected to the drain line 65, and the first drain valve 66 is provided on the upstream side (casing 51 side) of the connection portion of the drain line 65 with the suction line 68.
  • a second drain valve 67 is provided on the side (the drainage treatment facility side).
  • the vacuum valve 69 is provided closer to the inlet line 32 a than the connecting portion of the suction line 68 with the drain line 65.
  • part of the condenser 13, the strainer 14, the condensate pump 15, the first water supply line 31, the branch lines 32 and 33, and the second water supply line 34 is maintained at a vacuum pressure. Therefore, when the vent valve 62 is opened to open the outlet side chamber 54 to the atmosphere, and the vacuum valve 69 is opened to communicate the outlet side chamber 54 with the inlet line 32a by the suction line 68, the degree of vacuum of the inlet line 32a is the suction line It acts on the outlet side chamber 54 through 68. Then, in the casing 51 (outlet side chamber 54), the atmosphere is rapidly introduced from the vent line 61 to the inside, and the internal pressure of the casing 51 becomes higher than the pressure of the suction line 68 on the drain discharge side of the casing 51. The treated water inside is sucked to the inlet line 32 a side through the suction line 68, and the water level of the treated water in the casing 51 decreases rapidly.
  • the casing 51 is provided with a water level detection and estimation device that detects the water level inside.
  • the water level detection and estimation apparatus includes a measurement line 70 having one end connected to the suction line 68 (the outlet side chamber 54), a water level gauge 71 connected to the end of the measurement line 70, and a measuring instrument provided on the measurement line 70. It has an on-off valve 72.
  • the measuring line 70 may be directly connected to the outlet side chamber 54 instead of the suction line 68 at one end. Therefore, when the measuring instrument side open / close valve 72 is opened, the casing 51 and the water level gauge 71 communicate with each other through the suction line 68 and the measuring line 70, and the water level gauge 71 can measure the water level in the casing 51.
  • the control device 73 is connected to the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the first drain valve 66, the second drain valve 67, the vacuum valve 69, the water level gauge 71, and the measuring instrument side open / close valve 72 And a control signal from an external operating device (not shown) can be input.
  • the controller 73 controls the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the first drain valve 66, and the second drain valve 67 according to the control signal from the operating device and the detection result of the water level gauge 71.
  • the vacuum valve 69 and the measuring instrument side open / close valve 72 can be controlled to open and close.
  • the treated water in the casing 51 is discharged.
  • the controller 73 closes the vacuum valve 69 and reversely
  • the wash valve 64 and each drain valve 66, 67 are opened. That is, the discharge operation of the treated water in the casing 51 and the foreign material removal and discharge operation from the screen 52 are continuously performed.
  • FIG. 2 is a flowchart showing the method of cleaning the strainer according to the first embodiment.
  • the first water supply line 31 connected to the condenser 13 is branched into branch lines 32 and 33, and the inlet valve 43 and the first strainer 41 are branched to the branch line 32.
  • an outlet valve 44, and the branch line 33 is provided with an inlet valve 45, a second strainer 42, and an outlet valve 46. Therefore, the first strainer 41 and the second strainer 42 are alternately used by alternately opening and closing the inlet valves 43, 45 and the outlet valves 44, 46.
  • the vent valve 62, the first drain valve 66, the second drain valve 67, the vacuum valve 69, and the measuring device side open / close valve 72 are closed in the use state of the strainer, that is, the water flowing state.
  • step S11 the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to supply water to the second strainer 42, and cleaning is performed in step S12.
  • the inlet valve 43 and the outlet valve 44 of the first (in use) first strainer 41 are closed to stop water flow to the first strainer 41.
  • step S13 the vent valve 62 is opened to open the outlet side chamber 54 of the casing 51 to the atmosphere, whereby the inside of the casing 51 (inlet side chamber 53 and outlet side chamber 54) Introduce ambient air to
  • step S14 the measuring instrument side open / close valve 72 is opened to connect the casing 51 (outlet side chamber 54) and the water level gauge 71, and the water level gauge 71 can measure the water level of the treated water in the casing 51.
  • step S15 the vacuum valve 69 is opened, and the outlet side chamber 54 and the inlet line 32a are communicated by the suction line 68.
  • the degree of vacuum of the inlet line 32 a acts on the outlet side chamber 54 through the suction line 68, and the pressure of the outlet side chamber 54 becomes relatively higher than the pressure of the suction line 68. Therefore, when the treated water in the outlet side chamber 54 flows from the suction line 68 to the inlet line 32a, the water level in the casing 51 decreases.
  • the treated water in the outlet side chamber 54 is filtered water that has been filtered through the screen 52, even if it flows into the inlet line 32a, the condensate does not become dirty.
  • the control device 73 grasps the water level of the treated water in the casing 51 measured by the water level meter 71, and determines in step S16 whether the water level in the casing 51 has dropped to a predetermined water level. There is. Here, if it is determined that the water level in casing 51 has not dropped to the predetermined water level (No), this process is continued, and if it is determined that the water level in casing 51 has dropped to the predetermined water level (Yes), step Transfer to S17. In step S17, the vacuum valve 69 is closed to shut off the communication between the outlet side chamber 54 and the inlet line 32a by the suction line 68, and in step S18, the measuring device side on-off valve 72 is closed. Stop measuring the water level of the treated water.
  • step S19 the first drain valve 66 and the second drain valve 67 are opened, so that drainage of the treated water in the casing 51 from the inlet side chamber 53 by the drain line 65 is enabled.
  • step S20 by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed. Then, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 into the drain line 65 together with the water supply, and is discharged to the drainage treatment facility to be treated.
  • step S21 it is determined whether a predetermined time set in advance has passed since the backwash valve 64 was opened.
  • the predetermined time is the cleaning time of the screen 52, and the cleaning time capable of removing most foreign matter from the screen 52 is confirmed in advance by experiment or the like.
  • this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process proceeds to step S22.
  • the controller 73 closes the backwash valve 64 in step S22, closes the first drain valve 66 and the second drain valve 67 in step S23, and closes the vent valve 62 in step S24. Then, in step S25, a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13 is opened to remove the air in the casing 51 to make a vacuum state. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
  • the vent line 61 connected to the outlet side chamber 54, the vent valve 62 provided on the vent line 61, and the outlet side chamber 54 are connected to wash water.
  • a differential pressure generator for adjusting the internal pressure of the casing 51 higher than the pressure of the suction line 68.
  • the outlet side chamber 54 is opened to the atmosphere by the vent valve 62 and the internal pressure of the casing 51 is adjusted to be higher than the pressure of the suction line 68 by the differential pressure generator, the treated water in the casing 51 is It flows and the water level in casing 51 falls. Thereafter, when the water level reaches a predetermined level, the vacuum valve 69 is closed and the backwash valve 64 is opened to supply flush water from the backwash line 63 to the outlet side chamber 54 and open the drain valves 66 and 67, The foreign matter adhering to the screen 52 is removed, and the foreign matter is discharged from the inlet side chamber 53 to the drain line 65.
  • the treated water in the casing 51 can be discharged to the suction line 68 at an early stage. Can be shortened to improve processing efficiency. Further, since the cleaning process time of the strainer 14 can be shortened, the strainer 14 (41, 42) can be coped with a small size by increasing the number of times of alternately cleaning the respective strainers 41, 42, so the manufacturing cost Can be reduced.
  • a vent line 61 connected to the outlet side chamber 54, a vent valve 62 provided on the vent line 61, a suction line 68, and a suction line 68 are provided. And a vacuum valve 69. Therefore, when the vacuum valve 69 is opened, a suction force acts from the suction line 68 to the outlet side chamber 54, the internal pressure of the casing 51 becomes higher than the pressure of the suction line 68, and the treated water in the casing 51 is rapidly applied to the suction line 68. The water level in the casing 51 can be reduced early.
  • the first water supply line 31 is maintained at a vacuum pressure
  • the suction line 68 is connected to the inlet line 32 a on the upstream side of the inlet valve 43 in the first water supply line 31. . Therefore, only by connecting the suction line 68 to the inlet line 32a maintained at the vacuum pressure, the treated water in the casing 51 can be flowed to the suction line 68, and the water level in the casing 51 can be lowered early.
  • the suction line 68 is connected to the drain line 65, and the first drain valve 66 and the second drain are connected upstream and downstream of a connection portion of the drain line 65 with the suction line 68, respectively.
  • a valve 67 is provided. Therefore, after the water level in the casing 51 is lowered, the vacuum valve 69 is closed, and then the backwash valve 64 is opened to supply flush water from the backwash line 63 to the outlet side chamber 54 and the first drain valve 66 and When the second drain valve 67 is opened, the foreign matter adhering to the screen 52 is discharged from the inlet side chamber 53 to the drain line 65, and the treated water remaining in the suction line 68 can also be discharged.
  • the water level detection / estimation device for detecting or estimating the water level in the casing 51 and the vacuum valve 69 are closed when the water level in the casing 51 falls to a predetermined water level set in advance.
  • a controller 73 for opening the backwash valve 64 and the drain valves 66 and 67 is provided. Therefore, when the water level in the casing 51 drops to a predetermined water level, the drainage in the casing 51 and the removal of foreign matter are continuously performed in order to close the vacuum valve 69 and open the backwash valve 64 and the drain valves 66 and 67. be able to.
  • the treated water in the casing 51 can be discharged to the suction line 68 at an early stage. , 42) can be shortened to improve the processing efficiency.
  • the measurement line 70, the water level gauge 71, and the measuring device side open / close valve 72 are provided as the water level detection / estimation device for detecting the water level inside the casing 51, but this configuration is limited It is not a thing.
  • the control device 73 closes the vacuum valve 69 and opens the backwash valve 64 and the drain valves 66 and 67 when a predetermined time elapses after the vent valve 62 and the vacuum valve 69 are opened. Good.
  • FIG. 4 is a schematic view showing a strainer cleaning apparatus according to the second embodiment
  • FIG. 5 is a flowchart showing a strainer cleaning method according to the second embodiment.
  • the members having the same functions as those in the above-described embodiment are denoted by the same reference numerals, and detailed descriptions thereof will be omitted.
  • the vent line 61 is connected to the outlet side chamber 54, and the vent valve 62 is provided.
  • a backwash line 63 is connected to the outlet side chamber 54, and a backwash valve 64 is provided.
  • a drain line 65 is connected to the inlet side chamber 53, and a drain valve 66 is provided.
  • the first strainer 41 is provided with a differential pressure generator that adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65.
  • the differential pressure generator has a pressure line 81 connected to the backwash line 63, and a pressure valve 82 and a pressure pump (pressure device) 83 provided on the pressure line 81. That is, one end of the pressurizing line 81 is connected to the outlet side chamber 54 side of the backwashing valve 64 in the backwashing line 63, and the pressurizing valve 82 and the pressurizing pump 83 are provided.
  • the pressure line 81 may be directly connected to the outlet side chamber 54 or may be connected to the inlet side chamber 53.
  • the pressurization pump 83 was applied as a pressurization apparatus here, if there exists a pressurization air line in a plant, you may connect the pressurization line 81 to this pressurization air line.
  • the control device 73 is connected to the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82, and receives control signals from an external operating device (not shown). It is possible.
  • the controller 73 can control the opening and closing of the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82 in accordance with a control signal from the operating device.
  • the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82 are closed.
  • step S31 the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to the second strainer 42. Water is supplied, and in step S32, the inlet valve 43 and the outlet valve 44 of the first strainer 41 on the cleaning side (in use) are closed to stop the water supply to the first strainer 41.
  • step S33 the drain valve 66 is opened to allow the drain line 65 to discharge the treated water in the casing 51 from the inlet side chamber 53.
  • step S34 the pressurizing valve 82 is opened and the pressurizing pump 83 is driven to supply pressurized air to the outlet side chamber 54 through the pressurizing line 81 and the backwash line 63.
  • the pressure in the outlet side chamber 54 of the casing 51 becomes relatively higher than the pressure in the drain line 65. Therefore, when the treated water in the casing 51 is discharged from the inlet side chamber 53 by the drain line 65, the water level in the casing 51 decreases.
  • step S35 it is determined whether or not a predetermined time set in advance has elapsed since the pressurizing valve 82 was opened.
  • the predetermined time is a discharge time during which the treated water in the casing 51 is discharged, and is previously confirmed by an experiment or the like.
  • this process is continued, and it is determined that the predetermined time has elapsed since the pressurization valve 82 was opened (Yes) Then, the process proceeds to step S36.
  • step S36 the pressurizing valve 82 is closed and the driving of the pressurizing pump 83 is stopped.
  • step S37 by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed.
  • step S38 it is determined whether or not a predetermined time (washing time) set in advance has passed after the backwashing valve 64 is opened.
  • a predetermined time washing time
  • this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process moves to step S39.
  • the controller 73 closes the backwash valve 64 in step S39, and opens the vent valve 62 in step S40. Thereby, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 to the drain line 65 together with the washing water, and is discharged to the drainage treatment facility to be treated.
  • step S41 it is determined whether or not the opening time of the vent valve 62 has passed a preset predetermined time suitable for discharging the foreign matter and the water supply. If it is determined (No) that the predetermined time has not elapsed since the vent valve 62 was opened, this process is continued, and if it is determined (Yes) that the predetermined time has elapsed, the vent valve 62 is determined in step S42. Is closed, and the drain valve 66 is closed in step S43. Then, in step S44, a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13 is opened to remove the air in the casing 51 to make it into a vacuum state. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
  • the pressure line 81 connected to the outlet side chamber 54 and the pressure valve 82 provided on the pressure line 81 are provided as a differential pressure generator. There is.
  • the pressurizing valve 82 when the pressurizing valve 82 is opened in a state where the drain line 65 is opened by the drain valve 66, the internal pressure of the casing 51 becomes higher than the pressure of the drain line 65 by supplying pressurized air into the casing 51, The treated water in the casing 51 flows to the drain line 65, and the water level in the casing 51 decreases.
  • the backwashing valve 64 is opened and washing water is supplied from the backwashing line 63 to the outlet side chamber 54, the foreign matter adhering to the screen 52 is removed, and the foreign matter is discharged from the inlet side chamber 53 to the drain line 65. Ru.
  • the treated water in the casing 51 can be discharged to the drain line 65 at an early stage, and the strainer The processing time can be improved by shortening the cleaning process time of 14. Further, the water level in the casing 51 can be reduced early by only connecting the pressure line 81 to the outlet side chamber 54.
  • the pressure line 81 is provided with a pressure pump 83 as a pressure device. Therefore, only by providing the pressurizing pump 83 in the pressurizing line 81, the treated water in the casing 51 can be flowed to the drain line 65, and the water level in the casing 51 can be reduced early.
  • FIG. 6 is a schematic view showing a strainer cleaning apparatus according to the third embodiment
  • FIG. 7 is a flowchart showing a strainer cleaning method according to the third embodiment.
  • the members having the same functions as those in the above-described embodiment are denoted by the same reference numerals, and detailed descriptions thereof will be omitted.
  • a vent line 61 is connected to the outlet side chamber 54, and a vent valve 62 is provided in the vent line 61.
  • the backwash line 63 is connected to the outlet side chamber 54, and the backwash line 63 is provided with a backwash valve 64.
  • a drain line 65 is connected to the inlet side chamber 53, and a first drain valve 66 and a second drain valve 67 are provided in series in the drain line 65.
  • the first strainer 41 is provided with a differential pressure generator that adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65.
  • the differential pressure generator has a pressure line 81 connected to the backwash line 63 and a pressure valve 82 and a pressure pump 83 provided on the pressure line 81. Further, the differential pressure generator has a suction line 68 connected to the outlet side chamber 54 of the casing 51 and a vacuum valve 69 provided in the suction line 68.
  • step S 51 the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to the second strainer 42. Water is supplied, and in step S52, the inlet valve 43 and the outlet valve 44 of the first strainer 41 on the cleaning side (in use) are closed to stop the water supply to the first strainer 41.
  • step S53 the pressurizing valve 82 is opened and the pressurizing pump 83 is driven to supply pressurized air to the outlet side chamber 54 through the pressurizing line 81 and the backwash line 63.
  • step S54 the measuring instrument side open / close valve 72 is opened to communicate the casing 51 (outlet side chamber 54) with the water level gauge 71, and the water level gauge 71 can measure the water level of the treated water.
  • step S55 the vacuum valve 69 is opened, and the outlet side chamber 54 and the inlet line 32a are communicated by the suction line 68.
  • the pressurized air is supplied to the outlet side chamber 54, whereby the pressure in the outlet side chamber 54 of the casing 51 becomes high.
  • the pressure of the outlet side chamber 54 of the casing 51 is also increased by the degree of vacuum of the inlet line 32 a acting on the outlet side chamber 54 through the suction line 68.
  • the pressure in the outlet side chamber 54 of the casing 51 becomes relatively higher than the pressure in the suction line 68. Therefore, when the treated water in the outlet side chamber 54 flows from the suction line 68 to the inlet line 32a, the water level in the casing 51 is rapidly reduced.
  • control device 73 determines whether the water level in casing 51 has dropped to a predetermined water level. Here, if it is determined that the water level in casing 51 has not dropped to the predetermined water level (No), this process is continued, and if it is determined that the water level in casing 51 has dropped to the predetermined water level (Yes), step Transfer to S57.
  • step S57 the pressurizing valve 82 is closed and the driving of the pressurizing pump 83 is stopped.
  • the vacuum valve 69 is closed to shut off the communication between the outlet side chamber 54 and the inlet line 32a by the suction line 68, and in step S59, the measuring device side on-off valve 72 is closed. Stop measuring the level of treated water in 51.
  • step S60 the first drain valve 66 and the second drain valve 67 are opened to allow the drain line 65 to discharge the treated water in the casing 51 from the inlet side chamber 53.
  • step S61 by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed.
  • step S62 it is determined whether a predetermined time set in advance has passed since the backwash valve 64 was opened.
  • this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process moves to step S63.
  • the control device 73 closes the backwash valve 64 in step S63, and opens the vent valve 62 in step S64. Thereby, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 to the drain line 65 together with the washing water, and is discharged to the drainage treatment facility to be treated.
  • step S65 it is determined whether the opening time of the vent valve 62 has passed a predetermined time set in advance that is appropriate for discharging the foreign matter and the water supply. If it is determined (No) that the predetermined time has not elapsed since the vent valve 62 was opened, this process is continued, and if it is determined (Yes) that the predetermined time has elapsed, the vent valve 62 is determined in step S66. Are closed, and the first drain valve 66 and the second drain valve 67 are closed in step S67. Then, in step S68, the air in the casing 51 is removed to be in a vacuum state by opening a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
  • a balance valve not shown
  • the suction line 68 connected to the outlet side chamber 54 and the vacuum valve 69 provided on the suction line 68 are provided as a differential pressure generating device, and the outlet A pressure line 81 connected to the side chamber 54 and a pressure valve 82 provided on the pressure line 81 are provided.
  • the treated water in the casing 51 can be made into the suction line early. It is possible to discharge and shorten the cleaning processing time of the strainer 14 to improve the processing efficiency.
  • the vent valve 62 is opened for a predetermined time after the backwash valve 64 is closed, but the backwash valve 64 is opened after the pressurizing valve 82 is closed.
  • the vent valve 62 may be closed after a predetermined time has elapsed after the vent valve 62 has been opened and the backwash valve 64 has been closed. According to this configuration, the opening time of the vent valve 62 can be further shortened.
  • the vent valve 62 is opened and drained from the drain line 65 in order to drain out the foreign matter and flush water generated by the backwash line 63.
  • the pressure valve 82 is opened, and pressure from the pressure line 81 causes foreign matter The washing water may be discharged. As a result, it is possible to discharge the foreign matter and the washing water more quickly than the discharge by the vent line 61.
  • automatic control is performed by the control device 73.
  • manual control may be performed.
  • the first water supply line 31 connected to the condenser 13 is branched into two branch lines 32 and 33, and the inlet valve 43 and the first strainer 41 are connected to the branch line 32.
  • the outlet valve 44 is provided, and the inlet valve 45, the second strainer 42, and the outlet valve 46 are provided in the branch line 33.
  • the number of branches is not limited to two and may be three or more.
  • the strainer cleaning apparatus and method of the present invention have been described as applied to the water supply system of a thermal power plant, but the water supply system of a nuclear power plant or a geothermal power plant, or It can also be applied to other water supply systems.

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Abstract

The present invention provides a strainer cleaning device and method comprising: a vent line (61) connected to an outlet-side chamber (54); a vent valve (62) provided in the vent line (61); a backwash line (63) connected to the outlet-side chamber (54) and capable of supplying cleaning water; a backwash valve (64) provided in the backwash line (63); a drain line (65) connected to an inlet-side chamber (53) and capable of discharging foreign matter; drain valves (66, 67) provided in the drain line (65); and a differential pressure generation device for adjusting pressure in the casing (51) to a pressure higher than that in the drain line (65).

Description

ストレーナの洗浄装置及び方法Strainer cleaning apparatus and method
 本発明は、発電プラントの給水系統に設けられるストレーナの洗浄装置及び方法に関するものである。 The present invention relates to an apparatus and method for cleaning a strainer provided in a water supply system of a power plant.
 例えば、火力発電プラントでは、ボイラで燃料を燃焼させ、発生した燃焼ガスの熱エネルギをボイラ給水に伝熱することにより蒸気を発生させ、この蒸気により蒸気タービンを回転させることで、蒸気タービンの回転軸に連結された発電機を回転駆動して発電している。そして、蒸気タービンを回転させて仕事をした蒸気は、復水器にて、冷却水と熱交換して冷却することで凝縮して復水となり、復水ポンプによりボイラに給水として戻される。 For example, in a thermal power plant, steam is generated by burning fuel in a boiler, transferring heat energy of the generated combustion gas to boiler feed water to generate steam, and rotating the steam turbine with the steam, thereby rotating the steam turbine. The generator connected to the shaft is rotationally driven to generate electric power. Then, the steam that has been worked by rotating the steam turbine is condensed by heat exchange with cooling water and cooled by the condenser to be condensed water, and is returned to the boiler by the condensing water pump as water supply.
 このようなボイラ給水系統では、給水(蒸気)の循環系統に錆などの異物が混入することから、復水器の出口側に給水(復水)から異物を取り除くストレーナが設けられている。そして、このストレーナは、所定期間使用すると、異物により閉塞が発生することから、定期的に洗浄する必要がある。ストレーナの洗浄作業は、一般的に、ストレーナの入口側と出口側を閉止した状態とし、スクリーンに対してストレーナの吐出側から洗浄水を噴射する逆洗処理を実行するものであり、スクリーンから除去された異物を外部に排出している。このようなストレーナの洗浄装置としては、例えば、下記特許文献1に記載されたものがある。 In such a boiler water supply system, since foreign matter such as rust is mixed in the circulation system of the water supply (steam), a strainer for removing foreign matter from the water supply (condensed water) is provided on the outlet side of the condenser. Then, since this strainer is clogged by foreign matter when used for a predetermined period, it is necessary to periodically clean the strainer. Generally, the strainer is cleaned by closing the inlet side and outlet side of the strainer and performing a backwashing process to spray wash water from the discharge side of the strainer to the screen, and removing it from the screen Foreign substances are discharged to the outside. As such a strainer cleaning apparatus, for example, there is one described in Patent Document 1 below.
実開昭62-169276号公報Japanese Utility Model Publication No. 62-169276
 ところで、ストレーナを洗浄する前には、内部の復水を排出してからスクリーンに洗浄水を噴射する逆洗処理を実行する。ストレーナの排水時には、ストレーナの上部に設けたベントラインから大気を導入し、下部に設けた排水用ドレンラインから排水するが、ストレーナ内部の復水はドレンラインの圧力に対し、自重によって排出されるため、この排水作業に長時間を要してしまうという問題がある。 By the way, before the strainer is cleaned, the internal condensate is drained and then a backwashing process is performed in which washing water is sprayed onto the screen. When draining the strainer, air is introduced from the vent line provided at the upper part of the strainer and drained from the drain line for drain provided at the lower part, but the condensate inside the strainer is discharged by its own weight against the pressure of the drain line Therefore, there is a problem that this drainage work takes a long time.
 本発明は上述した課題を解決するものであり、洗浄処理時間の短縮化を図るストレーナの洗浄装置及び方法を提供することを目的とする。 The present invention solves the above-mentioned problems, and an object of the present invention is to provide a strainer cleaning apparatus and method for shortening the cleaning processing time.
 上記の目的を達成するための本発明のストレーナの洗浄装置は、ケーシングの内部がスクリーンにより入口側室と出口側室に区画され、前記入口側室に給水ラインが接続されて入口弁が設けられる一方、前記出口側室に前記給水ラインが接続されて出口弁が設けられるストレーナにおいて、前記出口側室に接続されて洗浄水を供給可能な逆洗ラインと、前記逆洗ラインに設けられる逆洗弁と、前記入口側室のドレン排出側に接続されて異物を排出可能なドレンラインと、前記ドレンラインに設けられるドレン弁と、前記ケーシングの内部圧力を前記ケーシングのドレン排出側の圧力より高く調整する差圧発生装置と、を備えることを特徴とするものである。 In the strainer cleaning apparatus of the present invention for achieving the above object, the inside of the casing is divided into an inlet side chamber and an outlet side chamber by a screen, and a water supply line is connected to the inlet side chamber to provide an inlet valve. In the strainer in which the water supply line is connected to the outlet side chamber and the outlet valve is provided, a backwash line connected to the outlet side chamber and capable of supplying washing water, a backwash valve provided on the backwash line, the inlet A differential pressure generating device for adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing, the drain line connected to the drain discharge side of the side chamber and capable of discharging foreign matter, the drain valve provided on the drain line And.
 従って、差圧発生装置によりケーシングのドレン排出側の圧力より高くなるように調整すると、ケーシング内の処理水がドレン排出側に流れてケーシング内の水位が低下する。ここで、逆洗弁を開放して洗浄水を逆洗ラインから出口側室に供給すると共にドレン弁を開放すると、ストレーナに付着していた異物が除去され、異物が入口側室からドレンラインに排出される。即ち、差圧発生装置によりケーシングの内部圧力をドレン排出側の圧力より高く調整することで、ケーシング内の処理水を早期に排出することができ、ストレーナの洗浄処理時間を短縮して処理効率を向上することができる。 Therefore, when the differential pressure generator adjusts the pressure to be higher than the pressure on the drain discharge side of the casing, the treated water in the casing flows to the drain discharge side to lower the water level in the casing. Here, when the backwash valve is opened to supply washing water from the backwash line to the outlet side chamber and the drain valve is opened, the foreign matter adhering to the strainer is removed, and the foreign matter is discharged from the inlet side chamber to the drain line Ru. That is, by adjusting the internal pressure of the casing to be higher than the pressure on the drain discharge side by the differential pressure generator, the treated water in the casing can be discharged at an early stage, and the processing time for cleaning the strainer is shortened. It can be improved.
 本発明のストレーナの洗浄装置では、前記差圧発生装置は、前記出口側室に接続されるベントラインと、前記ベントラインに設けられるベント弁と、前記出口側室のドレン排出側に接続される吸引ラインと、前記吸引ラインに設けられる吸引弁とを有することを特徴としている。 In the strainer cleaning apparatus according to the present invention, the differential pressure generator includes a vent line connected to the outlet side chamber, a vent valve provided on the vent line, and a suction line connected to the drain discharge side of the outlet side chamber. And a suction valve provided in the suction line.
 従って、吸引弁を開放すると、吸引ラインから出口側室に吸引力が作用し、ケーシングの内部圧力が吸引ラインの圧力より高くなり、ケーシング内の処理水を吸引ラインに急速に流すことができ、ケーシング内の水位を早期に低下させることができる。 Therefore, when the suction valve is opened, suction force acts from the suction line to the outlet side chamber, the internal pressure of the casing becomes higher than the pressure of the suction line, and treated water in the casing can be rapidly flowed to the suction line. Water level can be lowered early.
 本発明のストレーナの洗浄装置では、前記給水ラインは、真空圧状態に維持され、前記吸引ラインは、前記給水ラインにおける前記入口弁より上流側に接続され、前記吸引ラインの内部圧力より前記ケーシングの内部圧力を高くすることを特徴としている。 In the apparatus for cleaning a strainer of the present invention, the water supply line is maintained at a vacuum pressure, and the suction line is connected upstream of the inlet valve in the water supply line, and the internal pressure of the suction line It is characterized by raising the internal pressure.
 従って、吸引ラインを真空圧状態に維持された給水ラインに接続するだけで、ケーシング内の処理水を吸引ラインに流し、ケーシング内の水位を早期に低下させることができる。 Therefore, simply by connecting the suction line to the water supply line maintained at the vacuum pressure, the treated water in the casing can be flowed to the suction line and the water level in the casing can be reduced early.
 本発明のストレーナの洗浄装置では、前記吸引ラインは、前記ドレンラインに接続され、前記ドレンラインにおける前記吸引ラインとの接続部の上流側と下流側にそれぞれ前記ドレン弁として第1ドレン弁と第2ドレン弁が設けられることを特徴としている。 In the apparatus for cleaning a strainer according to the present invention, the suction line is connected to the drain line, and a first drain valve and a first drain valve are provided as the drain valve upstream and downstream of a connection portion of the drain line with the suction line. 2) It is characterized in that a drain valve is provided.
 従って、吸引ラインをドレンラインに接続することで、ケーシング内の水位が低下した後、逆洗弁を開放して洗浄水を逆洗ラインから出口側室に供給すると共に、第1ドレン弁及び第2ドレン弁を開放すると、ストレーナに付着していた異物が入口側室からドレンラインに排出されると共に、吸引ラインに残っている処理水も排出することができる。 Therefore, by connecting the suction line to the drain line, after the water level in the casing is lowered, the backwash valve is opened to supply wash water from the backwash line to the outlet side chamber, and the first drain valve and the second drain valve When the drain valve is opened, the foreign matter adhering to the strainer can be discharged from the inlet side chamber to the drain line, and the treated water remaining in the suction line can also be discharged.
 本発明のストレーナの洗浄装置では、前記ケーシング内の水位を検出または推定する水位検出推定装置が設けられることを特徴としている。 The apparatus for cleaning a strainer according to the present invention is characterized in that a water level detection and estimation device for detecting or estimating the water level in the casing is provided.
 従って、水位検出推定装置によりケーシング内の水位の低下がわかることから、吸引弁を閉止すると共に逆洗弁及びドレン弁を開放と、ケーシング内の排水と異物除去を連続して実施することができる。 Therefore, since the water level detection and estimation device indicates that the water level in the casing is lowered, the suction valve can be closed and the backwash valve and the drain valve can be opened to continuously carry out drainage and foreign matter removal in the casing. .
 本発明のストレーナの洗浄装置では、前記ケーシング内の水位を検出または推定する水位検出推定装置と、前記ケーシング内の水位が予め設定された所定水位まで低下すると前記吸引弁を閉止すると共に前記逆洗弁及び前記ドレン弁を開放する制御装置とが設けられることを特徴としている。 In the strainer cleaning apparatus according to the present invention, a water level detection and estimation device for detecting or estimating the water level in the casing, and closing the suction valve when the water level in the casing falls to a predetermined water level set in advance A valve and a control device for opening the drain valve are provided.
 従って、ケーシング内の水位が所定水位まで低下すると、吸引弁を閉止すると共に逆洗弁及びドレン弁を開放するため、ケーシング内の排水と異物除去を連続して実施することができる。 Therefore, when the water level in the casing drops to a predetermined water level, the suction valve is closed and the backwash valve and the drain valve are opened, so that drainage and foreign matter removal in the casing can be performed continuously.
 本発明のストレーナの洗浄装置では、前記差圧発生装置は、前記入口側室または前記出口側室に接続される加圧ラインと、前記加圧ラインに設けられる加圧弁とを有することを特徴としている。 In the strainer cleaning apparatus of the present invention, the differential pressure generating device is characterized by having a pressure line connected to the inlet side chamber or the outlet side chamber, and a pressure valve provided to the pressure line.
 従って、加圧弁を開放すると、加圧ラインから入口側室に加圧力が作用することとなり、ケーシングの内部圧力がドレンラインの圧力より高くなり、ケーシング内の処理水をドレンラインに流すことができ、入口側室に加圧ラインを接続するだけでケーシング内の水位を早期に低下させることができる。 Therefore, when the pressurizing valve is opened, pressurizing force acts on the inlet side chamber from the pressurizing line, the internal pressure of the casing becomes higher than the pressure of the drain line, and the treated water in the casing can flow to the drain line. The water level in the casing can be reduced early simply by connecting a pressure line to the inlet side chamber.
 本発明のストレーナの洗浄装置では、前記加圧ラインは、加圧装置に接続され、前記ドレンラインの圧力より前記ケーシングの内部圧力を高くすることを特徴としている。 In the strainer cleaning device according to the present invention, the pressurizing line is connected to a pressurizing device, and the internal pressure of the casing is made higher than the pressure of the drain line.
 従って、加圧ラインに加圧装置を接続するだけで、ケーシング内の処理水をドレンラインに流し、ケーシング内の水位を早期に低下させることができる。 Therefore, only by connecting the pressurizing device to the pressurizing line, the treated water in the casing can be flowed to the drain line, and the water level in the casing can be reduced early.
 本発明のストレーナの洗浄装置では、前記差圧発生装置は、前記加圧ラインが加圧装置に接続され、前記出口側室のドレン排出側に接続される吸引ラインと、前記吸引ラインに設けられる吸引弁とを有し、前記吸引ラインの圧力より前記ケーシングの内部圧力を高くすることを特徴としている。 In the strainer cleaning apparatus according to the present invention, the differential pressure generating device has a suction line connected to the pressure discharge device and the suction line connected to the drain side of the outlet side chamber, and suction provided to the suction line. And a valve, which is characterized in that the internal pressure of the casing is higher than the pressure of the suction line.
 従って、吸引弁を開放すると、吸引ラインから出口側室に吸引力が作用し、ケーシングの内部圧力が吸引ラインの圧力より高くなり、ケーシング内の処理水を吸引ラインに急速に流すことができ、ケーシング内の水位を早期に低下させることができる。 Therefore, when the suction valve is opened, suction force acts from the suction line to the outlet side chamber, the internal pressure of the casing becomes higher than the pressure of the suction line, and treated water in the casing can be rapidly flowed to the suction line. Water level can be lowered early.
 本発明のストレーナの洗浄装置では、前記給水ラインは、真空圧状態に維持され、前記吸引ラインは、前記給水ラインにおける前記入口弁より上流側に接続されることを特徴としている。 In the strainer cleaning apparatus according to the present invention, the water supply line is maintained at a vacuum pressure, and the suction line is connected upstream of the inlet valve in the water supply line.
 従って、吸引ラインを真空圧状態に維持された給水ラインに接続するだけで、ケーシング内の処理水を吸引ラインに流し、ケーシング内の水位を早期に低下させることができる。 Therefore, simply by connecting the suction line to the water supply line maintained at the vacuum pressure, the treated water in the casing can be flowed to the suction line and the water level in the casing can be reduced early.
 本発明のストレーナの洗浄装置では、前記吸引ラインは、前記ドレンラインに接続され、前記ドレンラインにおける前記吸引ラインとの接続部の上流側と下流側にそれぞれ前記ドレン弁として第1ドレン弁と第2ドレン弁が設けられることを特徴としている。 In the apparatus for cleaning a strainer according to the present invention, the suction line is connected to the drain line, and a first drain valve and a first drain valve are provided as the drain valve upstream and downstream of a connection portion of the drain line with the suction line. 2) It is characterized in that a drain valve is provided.
 従って、吸引ラインをドレンラインに接続することで、ケーシング内の水位が低下した後、逆洗弁を開放して洗浄水を逆洗ラインから出口側室に供給すると共に、第1ドレン弁及び第2ドレン弁を開放すると、ストレーナに付着していた異物が入口側室からドレンラインに排出されると共に、吸引ラインに残っている処理水も排出することができる。 Therefore, by connecting the suction line to the drain line, after the water level in the casing is lowered, the backwash valve is opened to supply wash water from the backwash line to the outlet side chamber, and the first drain valve and the second drain valve When the drain valve is opened, the foreign matter adhering to the strainer can be discharged from the inlet side chamber to the drain line, and the treated water remaining in the suction line can also be discharged.
 本発明のストレーナの洗浄装置では、前記ケーシング内の水位を検出または推定する水位検出推定装置が設けられることを特徴としている。 The apparatus for cleaning a strainer according to the present invention is characterized in that a water level detection and estimation device for detecting or estimating the water level in the casing is provided.
 従って、水位検出推定装置によりケーシング内の水位の低下がわかることから、吸引弁を閉止すると共に逆洗弁及びドレン弁を開放と、ケーシング内の排水と異物除去を連続して実施することができる。 Therefore, since the water level detection and estimation device indicates that the water level in the casing is lowered, the suction valve can be closed and the backwash valve and the drain valve can be opened to continuously carry out drainage and foreign matter removal in the casing. .
 本発明のストレーナの洗浄装置では、前記ケーシング内の水位が予め設定された所定水位まで低下すると前記吸引弁を閉止すると共に前記逆洗弁及び前記ドレン弁を開放する制御装置とが設けられることを特徴としている。 In the strainer cleaning apparatus according to the present invention, there is provided a control device for closing the suction valve and opening the backwash valve and the drain valve when the water level in the casing falls to a predetermined water level set in advance. It is characterized.
 従って、ケーシング内の水位が所定水位まで低下すると、吸引弁を閉止すると共に逆洗弁及びドレン弁を開放するため、ケーシング内の排水と異物除去を連続して実施することができる。 Therefore, when the water level in the casing drops to a predetermined water level, the suction valve is closed and the backwash valve and the drain valve are opened, so that drainage and foreign matter removal in the casing can be performed continuously.
 また、本発明のストレーナの洗浄方法は、ケーシングの内部がスクリーンにより入口側室と出口側室に区画され、前記入口側室に給水ラインが接続されて入口弁が設けられる一方、前記出口側室に前記給水ラインが接続されて出口弁が設けられるストレーナにおいて、前記入口弁と前記出口弁を閉止する工程と、前記ケーシングの内部圧力を前記ケーシングのドレン排出側の圧力より高く調整する工程と、前記ケーシング内の水位が予め設定された所定水位まで低下すると前記出口側室に洗浄水を供給すると共に前記ドレンラインを開放する工程と、を有することを特徴とするものである。 In the strainer cleaning method according to the present invention, the inside of the casing is divided into an inlet side chamber and an outlet side chamber by a screen, and a water supply line is connected to the inlet side chamber to provide an inlet valve. In a strainer in which an outlet valve is provided, the steps of closing the inlet valve and the outlet valve, adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing, and Supplying flush water to the outlet side chamber and opening the drain line when the water level falls to a predetermined water level set in advance.
 従って、ケーシングの内部圧力をケーシングのドレン排出側の圧力より高く調整することで、ケーシング内の処理水を早期にドレンラインに排出することができ、ストレーナの洗浄処理時間を短縮して処理効率を向上することができる。 Therefore, by adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing, the treated water in the casing can be discharged early to the drain line, and the treatment time for cleaning the strainer is shortened and the treatment efficiency is improved. It can be improved.
 本発明のストレーナの洗浄装置及び方法によれば、ケーシングの内部圧力をドレン排出側の圧力より高く調整するので、ケーシング内の処理水を早期に排出することができ、ストレーナの洗浄処理時間を短縮することができる。 According to the apparatus and method for cleaning a strainer of the present invention, the internal pressure of the casing is adjusted to be higher than the pressure on the drain discharge side, so the treated water in the casing can be discharged early, thereby shortening the cleaning processing time of the strainer. can do.
図1は、第1実施形態のストレーナの洗浄装置を表す概略図である。FIG. 1 is a schematic view showing a cleaning device of a strainer according to a first embodiment. 図2は、第1実施形態のストレーナの洗浄方法を表すフローチャートである。FIG. 2 is a flowchart showing the method of cleaning the strainer according to the first embodiment. 図3は、火力発電プラントを表す概略図である。FIG. 3 is a schematic view showing a thermal power plant. 図4は、第2実施形態のストレーナの洗浄装置を表す概略図である。FIG. 4 is a schematic view showing a cleaning device of a strainer according to a second embodiment. 図5は、第2実施形態のストレーナの洗浄方法を表すフローチャートである。FIG. 5 is a flowchart showing a method of cleaning a strainer according to a second embodiment. 図6は、第3実施形態のストレーナの洗浄装置を表す概略図である。FIG. 6 is a schematic view showing a strainer cleaning apparatus according to a third embodiment. 図7は、第3実施形態のストレーナの洗浄方法を表すフローチャートである。FIG. 7 is a flowchart showing a method of cleaning a strainer according to a third embodiment.
 以下に添付図面を参照して、本発明に係るストレーナの洗浄装置及び方法の好適な実施形態を詳細に説明する。なお、この実施形態により本発明が限定されるものではなく、また、実施形態が複数ある場合には、各実施形態を組み合わせて構成するものも含むものである。 Hereinafter, preferred embodiments of the apparatus and method for cleaning a strainer according to the present invention will be described in detail with reference to the accompanying drawings. Note that the present invention is not limited by the embodiments, and in the case where there are a plurality of embodiments, the present invention also includes those configured by combining the respective embodiments.
[第1実施形態]
 図3は、火力発電プラントを表す概略図である。
First Embodiment
FIG. 3 is a schematic view showing a thermal power plant.
 第1実施形態の火力発電プラントは、燃料を燃焼させ、燃焼により発生した熱で蒸気を生成し、生成した蒸気により蒸気タービンを回転させることで、蒸気タービンに接続される発電機を駆動して電力を発生させるものである。 The thermal power plant according to the first embodiment burns fuel, generates steam with heat generated by combustion, and rotates a steam turbine with the produced steam to drive a generator connected to the steam turbine. It generates power.
 図3に示すように、火力発電プラント10は、ボイラ11と、蒸気タービン12と、復水器13と、ストレーナ14と、復水ポンプ15と、低圧給水加熱器16と、脱気器17と、高圧給水加熱器18と、発電機19とを備えている。 As shown in FIG. 3, the thermal power plant 10 includes a boiler 11, a steam turbine 12, a condenser 13, a strainer 14, a condensate pump 15, a low pressure feed water heater 16, and a deaerator 17. , A high pressure feed water heater 18 and a generator 19.
 ボイラ11は、例えば、コンベンショナルボイラが用いられており、燃料としての微粉炭を燃焼バーナにより燃焼させ、この燃焼により発生した熱を伝熱管として機能する火炉壁管21を用いて回収することができる。蒸気タービン12は、高圧タービン22と、中圧タービン23と、低圧タービン24とを有し、各タービン22,23,24は、回転軸となるロータ25によって一体回転可能に連結されている。 For example, a conventional boiler is used for the boiler 11, and it is possible to burn pulverized coal as a fuel by a combustion burner and recover heat generated by this combustion using a furnace wall pipe 21 functioning as a heat transfer pipe . The steam turbine 12 has a high pressure turbine 22, an intermediate pressure turbine 23, and a low pressure turbine 24. The turbines 22, 23, 24 are integrally rotatably connected by a rotor 25 serving as a rotation shaft.
 高圧タービン22は、その流入側にボイラ11の火炉壁管21からの主蒸気ライン26が接続され、その流出側にボイラ11の再熱器(図示略)に至る低温再熱蒸気ライン27が接続されている。高圧タービン22は、主蒸気ライン26から供給される蒸気によって回転し、使用後の蒸気を低温再熱蒸気ライン27から排出する。中圧タービン23は、その流入側にボイラ11の再熱器からの高温再熱蒸気ライン28が接続され、その流出側に低圧タービン24に至る蒸気ライン29が接続されている。中圧タービン23は、高温再熱蒸気ライン28から供給される再熱された蒸気によって回転し、使用後の蒸気を蒸気ライン29から低圧タービン24へ向けて排出する。低圧タービン24は、その流入側に蒸気ライン29が接続され、その流出側に復水器13が接続されている。低圧タービン24は、蒸気ライン29から供給される蒸気によって回転し、使用後の蒸気を復水器13へ向けて排出する。発電機19は、高圧タービン22、中圧タービン23、低圧タービン24の回転がロータ25を介して伝達され、回転駆動して発電する。 In the high pressure turbine 22, the main steam line 26 from the furnace wall pipe 21 of the boiler 11 is connected to the inflow side, and the low temperature reheat steam line 27 leading to the reheater (not shown) of the boiler 11 is connected to the outflow side. It is done. The high pressure turbine 22 is rotated by the steam supplied from the main steam line 26 and discharges the used steam from the low temperature reheat steam line 27. The high pressure reheat steam line 28 from the reheater of the boiler 11 is connected to the inflow side of the intermediate pressure turbine 23, and the steam line 29 leading to the low pressure turbine 24 is connected to the outflow side. The medium pressure turbine 23 is rotated by the reheated steam supplied from the high temperature reheat steam line 28 and discharges the used steam from the steam line 29 toward the low pressure turbine 24. The steam line 29 is connected to the low pressure turbine 24 at the inflow side, and the condenser 13 is connected to the outflow side. The low pressure turbine 24 is rotated by the steam supplied from the steam line 29 and discharges the used steam to the condenser 13. In the generator 19, the rotations of the high pressure turbine 22, the intermediate pressure turbine 23, and the low pressure turbine 24 are transmitted through the rotor 25 and rotationally driven to generate electric power.
 復水器13は、低圧タービン24から排出される蒸気を、冷却水が流れる冷却ラインに接触させることによって凝縮して水(復水)に戻すものである。復水器13で生成された復水は、ストレーナ14により異物が除去されてから復水ポンプ15により低圧給水加熱器16へ向けて供給される。復水器13の流出側に接続された第1給水ライン31は、2つの分岐ライン32,33に分岐され、再び集合して第2給水ライン34となり、ボイラ11の火炉壁管21に接続されている。ストレーナ14は、第1ストレーナ41と第2ストレーナ42とから構成される。第1ストレーナ41は、分岐ライン32に設けられており、流入側に入口弁43が設けられ、流出側に出口弁44が設けられている。第2ストレーナ42は、分岐ライン33に設けられており、流入側に入口弁45が設けられ、流出側に出口弁46が設けられている。なお、第1ストレーナ41の入口弁43と出口弁44は、図で白抜きとして開放状態を示し、第2ストレーナ42の入口弁45と出口弁46は黒塗りとして弁が閉止状態であることを示している。即ち、第1ストレーナ41は通水状態で、第2ストレーナ42は通水が遮断状態であることを示している。 The condenser 13 condenses the steam discharged from the low pressure turbine 24 back to water (condensed water) by coming into contact with a cooling line through which the cooling water flows. The condensed water generated by the condenser 13 is supplied to the low pressure feed water heater 16 by the condensate pump 15 after the foreign matter is removed by the strainer 14. The first water supply line 31 connected to the outlet side of the condenser 13 is branched into two branch lines 32 and 33, collected again to form a second water supply line 34, and connected to the furnace wall pipe 21 of the boiler 11 ing. The strainer 14 is composed of a first strainer 41 and a second strainer 42. The first strainer 41 is provided in the branch line 32, the inlet valve 43 is provided on the inflow side, and the outlet valve 44 is provided on the outflow side. The second strainer 42 is provided in the branch line 33, the inlet valve 45 is provided on the inflow side, and the outlet valve 46 is provided on the outflow side. In the drawing, the inlet valve 43 and the outlet valve 44 of the first strainer 41 are shown as being white in the drawing, and the inlet valve 45 and the outlet valve 46 of the second strainer 42 are shown as being black. It shows. That is, the first strainer 41 is in the water flowing state, and the second strainer 42 is in the water blocking state.
 復水ポンプ15と低圧給水加熱器16と脱気器17と高圧給水加熱器18は、第2分岐ライン34に直列に設けられている。低圧給水加熱器16は、復水を低圧の状態で加熱する。加熱された水は、低圧給水加熱器16から脱気器17へ向けて供給される。脱気器17は、低圧給水加熱器16から供給された復水から溶存酸素や不凝結ガス(アンモニアガス)などの不純物を除去する。脱気された水は、脱気器17から高圧給水加熱器18へ向けて供給される。高圧給水加熱器18は、脱気された復水を高圧の状態で加熱する。加熱された復水は、高圧給水加熱器18から給水としてボイラ11の火炉壁管21へ向けて供給される。 The condensate pump 15, the low pressure feed water heater 16, the deaerator 17 and the high pressure feed water heater 18 are provided in series in the second branch line 34. The low pressure feed water heater 16 heats the condensed water at a low pressure. The heated water is supplied from the low pressure feed water heater 16 to the deaerator 17. The deaerator 17 removes impurities such as dissolved oxygen and non-condensable gas (ammonia gas) from the condensed water supplied from the low pressure feed water heater 16. Deaerated water is supplied from the deaerator 17 toward the high pressure feed water heater 18. The high pressure feed water heater 18 heats the degassed condensate under high pressure. The heated condensate is supplied from the high pressure feed water heater 18 toward the furnace wall pipe 21 of the boiler 11 as the feed water.
 なお、復水器13は、蒸気タービン12で使用された蒸気を冷却水により冷却し、凝縮させることで復水とし、体積を減らすことにより高い真空状態を作り、蒸気の流れをよくしてタービンの効率を向上させている。そのため、少なくとも、復水器13、ストレーナ14、復水ポンプ15までの第1給水ライン31と分岐ライン32,33と第2給水ライン34は、真空状態が維持されている。 In addition, the condenser 13 cools the steam used in the steam turbine 12 with cooling water and condenses it for condensation to reduce the volume to create a high vacuum state and improve the flow of the steam to make the turbine Improve the efficiency of Therefore, the vacuum state is maintained at least the condenser 13, the strainer 14, and the first water supply line 31, the branch lines 32 and 33, and the second water supply line 34 to the condensate pump 15.
 そのため、火力発電プラント10では、ボイラ11の火炉壁管21内を流通する水は、内部の火炎により加熱されて蒸気が生成され、生成された蒸気は、蒸気タービン12に供給される。蒸気タービン12に供給された蒸気は、高圧タービン22、中圧タービン23、低圧タービン24を順に流動して復水器13に流入する。このとき、蒸気タービン12は、流通した蒸気により回転することで、ロータ25を介して発電機19を回転駆動し、発電機19が電力を発生させる。復水器13に流入した蒸気は、冷却ラインによって凝縮されることで復水に戻される。復水器13で凝縮された復水は、ストレーナ14により異物が除去された後、低圧給水加熱器16、脱気器17、高圧給水加熱器18を通ってボイラ11の火炉壁管21内へ戻される。 Therefore, in the thermal power plant 10, the water flowing in the furnace wall pipe 21 of the boiler 11 is heated by the internal flame to generate steam, and the generated steam is supplied to the steam turbine 12. The steam supplied to the steam turbine 12 flows through the high pressure turbine 22, the intermediate pressure turbine 23, and the low pressure turbine 24 in order and flows into the condenser 13. At this time, the steam turbine 12 is rotated by the flowed steam, so that the generator 19 is rotationally driven via the rotor 25, and the generator 19 generates electric power. The steam flowing into the condenser 13 is returned to the condensate by being condensed by the cooling line. The condensate condensed by the condenser 13 is subjected to the low pressure feed water heater 16, the deaerator 17 and the high pressure feed water heater 18 into the furnace wall pipe 21 of the boiler 11 after the foreign matter is removed by the strainer 14. Will be returned.
 ここで、ストレーナ14について説明するが、このストレーナ14を構成する第1ストレーナ41と第2ストレーナ42は、各給水ライン31,34の間で並列に配置されてほぼ同様の構成をなすことから、第1ストレーナ41について詳細に説明する。図1は、第1実施形態のストレーナの洗浄装置を表す概略図である。 Here, although the strainer 14 will be described, since the first strainer 41 and the second strainer 42 constituting the strainer 14 are arranged in parallel between the water supply lines 31 and 34 and have substantially the same configuration, The first strainer 41 will be described in detail. FIG. 1 is a schematic view showing a cleaning device of a strainer according to a first embodiment.
 図1に示すように、第1ストレーナ41は、ケーシング51内にスクリーン(メッシュ)52が傾斜状態で配置されることで、内部が入口側室53と出口側室54とに区画されている。そして、入口側室53は、分岐ライン32における入口ライン32aの下流側端部が接続され、出口側室54に分岐ライン32における出口ライン32bの上流側端部が接続されている。入口ライン32aは、入口弁43が設けられ、出口ライン32bは、出口弁44が設けられている。 As shown in FIG. 1, the screen (mesh) 52 is disposed in an inclined state in the casing 51 so that the inside of the first strainer 41 is divided into an inlet side chamber 53 and an outlet side chamber 54. The inlet side chamber 53 is connected to the downstream end of the inlet line 32 a in the branch line 32, and the upstream end of the outlet line 32 b in the branch line 32 is connected to the outlet side chamber 54. The inlet line 32 a is provided with an inlet valve 43, and the outlet line 32 b is provided with an outlet valve 44.
 ケーシング51は、出口側室54にベントライン61が接続され、ベントライン61にベント弁62が設けられている。ベントライン61は、一端部が大気に開放されており、ベント弁62を閉止することでケーシング51内を密閉状態に維持し、開放することでケーシング51内を大気に連通する。なお。ベントライン61は、ケーシング51の入口側室53に接続してもよい。 In the casing 51, a vent line 61 is connected to the outlet side chamber 54, and a vent valve 62 is provided in the vent line 61. One end of the vent line 61 is open to the atmosphere, and the inside of the casing 51 is maintained in a sealed state by closing the vent valve 62, and the inside of the casing 51 is communicated to the atmosphere by opening the same. In addition. The vent line 61 may be connected to the inlet side chamber 53 of the casing 51.
 ケーシング51は、出口側室54に逆洗ライン63が接続され、逆洗ライン63に逆洗弁64が設けられている。逆洗ライン63は、一端部が第2給水ライン34(図3参照)に接続されており、逆洗弁64を開放することで、第2給水ライン34の給水を洗浄水として出口側室54内に供給することができる。また、ケーシング51は、入口側室53にドレンライン65が接続され、ドレンライン65に第1ドレン弁66と第2ドレン弁67が直列に設けられている。ドレンライン65は、一端部が図示しない排水処理設備に接続されており、各ドレン弁66,67を開放することで、入口側室53内の処理水や洗浄水を排水処理設備に排出することができる。 In the casing 51, the backwash line 63 is connected to the outlet side chamber 54, and the backwash line 63 is provided with a backwash valve 64. One end of the backwashing line 63 is connected to the second water supply line 34 (see FIG. 3), and by opening the backwashing valve 64, the water supply of the second water supply line 34 is used as cleaning water in the outlet side chamber 54. Can be supplied. Further, in the casing 51, the drain line 65 is connected to the inlet side chamber 53, and the first drain valve 66 and the second drain valve 67 are provided in series in the drain line 65. The drain line 65 is connected at one end to a waste water treatment facility (not shown), and the treated water and wash water in the inlet side chamber 53 can be discharged to the waste water treatment facility by opening the respective drain valves 66 and 67. it can.
 また、第1ストレーナ41は、ケーシング51の内部圧力をドレンライン65の圧力より高く調整する差圧発生装置が設けられている。差圧発生装置は、ケーシング51の出口側室54に接続され、ケーシング51のドレン排出側に設けられる吸引ライン68と、吸引ライン68に設けられる真空弁(吸引弁)69とを有している。即ち、吸引ライン68は、一端部がケーシング51の出口側室54に接続され、他端部が分岐ライン32を構成する入口ライン32aにおける入口弁43より上流側に接続されている。この場合、吸引ライン68は、ドレンライン65に接続されており、ドレンライン65における吸引ライン68との接続部の上流側(ケーシング51側)に第1ドレン弁66が設けられ、接続部より下流側(排水処理設備側)に第2ドレン弁67が設けられている。また、真空弁69は、吸引ライン68におけるドレンライン65との接続部より入口ライン32a側に設けられている。 Further, the first strainer 41 is provided with a differential pressure generating device which adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65. The differential pressure generator has a suction line 68 connected to the outlet side chamber 54 of the casing 51 and provided on the drain discharge side of the casing 51, and a vacuum valve (suction valve) 69 provided on the suction line 68. That is, one end of the suction line 68 is connected to the outlet side chamber 54 of the casing 51 and the other end is connected to the upstream side of the inlet valve 43 in the inlet line 32 a constituting the branch line 32. In this case, the suction line 68 is connected to the drain line 65, and the first drain valve 66 is provided on the upstream side (casing 51 side) of the connection portion of the drain line 65 with the suction line 68. A second drain valve 67 is provided on the side (the drainage treatment facility side). Further, the vacuum valve 69 is provided closer to the inlet line 32 a than the connecting portion of the suction line 68 with the drain line 65.
 前述したように、復水器13とストレーナ14と復水ポンプ15と第1給水ライン31と分岐ライン32,33と第2給水ライン34の一部が真空圧状態に維持されている。そのため、ベント弁62を開放して出口側室54を大気に開放し、真空弁69を開放して吸引ライン68により出口側室54と入口ライン32aとを連通すると、入口ライン32aの真空度が吸引ライン68を通して出口側室54に作用する。すると、ケーシング51(出口側室54)は、内部にベントライン61から急激に大気が導入されることで、ケーシング51の内部圧力がケーシング51のドレン排出側となる吸引ライン68の圧力より高くなり、内部の処理水が吸引ライン68を通して入口ライン32a側に吸引され、ケーシング51内の処理水の水位が急速に減少する。 As described above, part of the condenser 13, the strainer 14, the condensate pump 15, the first water supply line 31, the branch lines 32 and 33, and the second water supply line 34 is maintained at a vacuum pressure. Therefore, when the vent valve 62 is opened to open the outlet side chamber 54 to the atmosphere, and the vacuum valve 69 is opened to communicate the outlet side chamber 54 with the inlet line 32a by the suction line 68, the degree of vacuum of the inlet line 32a is the suction line It acts on the outlet side chamber 54 through 68. Then, in the casing 51 (outlet side chamber 54), the atmosphere is rapidly introduced from the vent line 61 to the inside, and the internal pressure of the casing 51 becomes higher than the pressure of the suction line 68 on the drain discharge side of the casing 51. The treated water inside is sucked to the inlet line 32 a side through the suction line 68, and the water level of the treated water in the casing 51 decreases rapidly.
 ケーシング51は、内部の水位を検出する水位検出推定装置が設けられている。水位検出推定装置は、一端部が吸引ライン68(出口側室54)に接続される計測ライン70と、計測ライン70の端部に接続される水位計71と、計測ライン70に設けられる計測器側開閉弁72とを有している。計測ライン70は、一端部を吸引ライン68ではなくて出口側室54に直接接続してもよい。そのため、計測器側開閉弁72を開放すると、ケーシング51と水位計71が吸引ライン68及び計測ライン70を通して連通し、水位計71は、ケーシング51内の水位を計測することができる。 The casing 51 is provided with a water level detection and estimation device that detects the water level inside. The water level detection and estimation apparatus includes a measurement line 70 having one end connected to the suction line 68 (the outlet side chamber 54), a water level gauge 71 connected to the end of the measurement line 70, and a measuring instrument provided on the measurement line 70. It has an on-off valve 72. The measuring line 70 may be directly connected to the outlet side chamber 54 instead of the suction line 68 at one end. Therefore, when the measuring instrument side open / close valve 72 is opened, the casing 51 and the water level gauge 71 communicate with each other through the suction line 68 and the measuring line 70, and the water level gauge 71 can measure the water level in the casing 51.
 制御装置73は、入口弁43、出口弁44、ベント弁62、逆洗弁64、第1ドレン弁66、第2ドレン弁67、真空弁69、水位計71、計測器側開閉弁72に接続されていると共に、外部の操作装置(図示略)からの制御信号が入力可能となっている。制御装置73は、操作装置からの制御信号や水位計71の検出結果に応じて入口弁43、出口弁44、ベント弁62、逆洗弁64、第1ドレン弁66、第2ドレン弁67、真空弁69、計測器側開閉弁72を開閉制御可能となっている。 The control device 73 is connected to the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the first drain valve 66, the second drain valve 67, the vacuum valve 69, the water level gauge 71, and the measuring instrument side open / close valve 72 And a control signal from an external operating device (not shown) can be input. The controller 73 controls the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the first drain valve 66, and the second drain valve 67 according to the control signal from the operating device and the detection result of the water level gauge 71. The vacuum valve 69 and the measuring instrument side open / close valve 72 can be controlled to open and close.
 例えば、第1ストレーナ41にて、入口弁43と出口弁44を閉止し、ベント弁62と真空弁69と計測器側開閉弁72を開放することで、ケーシング51内の処理水を排出しているとき、制御装置73は、水位計71が計測したケーシング51内の水位が予め設定された所定水位まで低下すると、つまり、ケーシング51内の処理水がなくなると、真空弁69を閉止すると共に逆洗弁64及び各ドレン弁66,67を開放する。即ち、ケーシング51内の処理水の排出作業と、スクリーン52からの異物除去及び排出作業を連続して実施する。 For example, by closing the inlet valve 43 and the outlet valve 44 in the first strainer 41 and opening the vent valve 62, the vacuum valve 69, and the measuring device side on-off valve 72, the treated water in the casing 51 is discharged. When the water level in the casing 51 measured by the water level gauge 71 falls to a predetermined level set in advance, that is, when the treated water in the casing 51 disappears, the controller 73 closes the vacuum valve 69 and reversely The wash valve 64 and each drain valve 66, 67 are opened. That is, the discharge operation of the treated water in the casing 51 and the foreign material removal and discharge operation from the screen 52 are continuously performed.
 ここで、第1実施形態のストレーナの洗浄装置による第1ストレーナ41の洗浄方法について説明する。図2は、第1実施形態のストレーナの洗浄方法を表すフローチャートである。 Here, a method of cleaning the first strainer 41 by the cleaning device of the strainer of the first embodiment will be described. FIG. 2 is a flowchart showing the method of cleaning the strainer according to the first embodiment.
 第1実施形態のストレーナの洗浄方法は、入口弁43と出口弁44を閉止する工程と、出口側室54を大気開放する工程と、ケーシング51の内部圧力を出口側室54に接続される吸引ライン68の圧力より高く調整する工程と、ケーシング51内の水位が所定水位まで低下すると出口側室54に洗浄水を供給すると共にドレンライン65を開放する工程とを有している。 In the strainer cleaning method according to the first embodiment, a step of closing the inlet valve 43 and the outlet valve 44, a step of opening the outlet side chamber 54 to the atmosphere, and a suction line 68 connected the internal pressure of the casing 51 to the outlet side chamber 54. And adjusting the pressure in the casing 51 to a predetermined level, and supplying drain water to the outlet side chamber 54 and opening the drain line 65.
 具体的に説明すると、図3に示すように、復水器13に接続される第1給水ライン31は、各分岐ライン32,33に分岐され、分岐ライン32に入口弁43と第1ストレーナ41と出口弁44が設けられ、分岐ライン33に入口弁45と第2ストレーナ42と出口弁46が設けられている。そのため、各入口弁43,45と出口弁44,46を交互に開閉することで、第1ストレーナ41と第2ストレーナ42を交互に使用する。ここでは、第2ストレーナ42が清掃済で待機状態にあり、使用中の第1ストレーナ41を待機状態として洗浄する場合について説明する。なお、ストレーナの使用状態、即ち、通水状態では、ベント弁62、第1ドレン弁66、第2ドレン弁67、真空弁69、計測器側開閉弁72は閉止状態である。 Specifically, as shown in FIG. 3, the first water supply line 31 connected to the condenser 13 is branched into branch lines 32 and 33, and the inlet valve 43 and the first strainer 41 are branched to the branch line 32. And an outlet valve 44, and the branch line 33 is provided with an inlet valve 45, a second strainer 42, and an outlet valve 46. Therefore, the first strainer 41 and the second strainer 42 are alternately used by alternately opening and closing the inlet valves 43, 45 and the outlet valves 44, 46. Here, the case where the second strainer 42 is cleaned and in the standby state and the first strainer 41 in use is cleaned in the standby state will be described. The vent valve 62, the first drain valve 66, the second drain valve 67, the vacuum valve 69, and the measuring device side open / close valve 72 are closed in the use state of the strainer, that is, the water flowing state.
 第1実施形態のストレーナの洗浄方法において、ステップS11にて、待機側の第2ストレーナ42の入口弁45及び出口弁46を開放して第2ストレーナ42に通水し、ステップS12にて、清掃側(使用中)の第1ストレーナ41の入口弁43及び出口弁44を閉止して第1ストレーナ41への通水を停止する。そして、図1及び図2に示すように、ステップS13にて、ベント弁62を開放してケーシング51の出口側室54を大気開放することで、ケーシング51の内部(入口側室53と出口側室54)に外気を導入する。 In the method of cleaning the strainer according to the first embodiment, in step S11, the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to supply water to the second strainer 42, and cleaning is performed in step S12. The inlet valve 43 and the outlet valve 44 of the first (in use) first strainer 41 are closed to stop water flow to the first strainer 41. Then, as shown in FIGS. 1 and 2, in step S13, the vent valve 62 is opened to open the outlet side chamber 54 of the casing 51 to the atmosphere, whereby the inside of the casing 51 (inlet side chamber 53 and outlet side chamber 54) Introduce ambient air to
 ステップS14にて、計測器側開閉弁72を開放してケーシング51(出口側室54)と水位計71を連通し、水位計71によりケーシング51内の処理水の水位を計測可能とする。そして、ステップS15にて、真空弁69を開放して吸引ライン68により出口側室54と入口ライン32aとを連通する。すると、入口ライン32aの真空度が吸引ライン68を通して出口側室54に作用し、出口側室54の圧力が吸引ライン68の圧力より相対的に高くなる。そのため、出口側室54内の処理水が吸引ライン68から入口ライン32aに流れることで、ケーシング51内の水位が減少する。なお、出口側室54内の処理水は、スクリーン52を通過してろ過処理されたろ過水であることから、入口ライン32aに流れ込んでも、復水が汚れることはない。 In step S14, the measuring instrument side open / close valve 72 is opened to connect the casing 51 (outlet side chamber 54) and the water level gauge 71, and the water level gauge 71 can measure the water level of the treated water in the casing 51. Then, in step S15, the vacuum valve 69 is opened, and the outlet side chamber 54 and the inlet line 32a are communicated by the suction line 68. Then, the degree of vacuum of the inlet line 32 a acts on the outlet side chamber 54 through the suction line 68, and the pressure of the outlet side chamber 54 becomes relatively higher than the pressure of the suction line 68. Therefore, when the treated water in the outlet side chamber 54 flows from the suction line 68 to the inlet line 32a, the water level in the casing 51 decreases. In addition, since the treated water in the outlet side chamber 54 is filtered water that has been filtered through the screen 52, even if it flows into the inlet line 32a, the condensate does not become dirty.
 制御装置73は、水位計71が計測しているケーシング51内の処理水の水位を把握しており、ステップS16にて、ケーシング51内の水位が所定水位レベルまで低下したかどうかを判定している。ここで、ケーシング51内の水位が所定水位レベルまで低下していないと判定(No)すると、この処理を継続し、ケーシング51内の水位が所定水位レベルまで低下したと判定(Yes)すると、ステップS17に移行する。ステップS17では、真空弁69を閉止して吸引ライン68による出口側室54と入口ライン32aとの連通を遮断し、ステップS18では、計測器側開閉弁72を閉止して水位計71によるケーシング51内の処理水の水位の計測を停止する。 The control device 73 grasps the water level of the treated water in the casing 51 measured by the water level meter 71, and determines in step S16 whether the water level in the casing 51 has dropped to a predetermined water level. There is. Here, if it is determined that the water level in casing 51 has not dropped to the predetermined water level (No), this process is continued, and if it is determined that the water level in casing 51 has dropped to the predetermined water level (Yes), step Transfer to S17. In step S17, the vacuum valve 69 is closed to shut off the communication between the outlet side chamber 54 and the inlet line 32a by the suction line 68, and in step S18, the measuring device side on-off valve 72 is closed. Stop measuring the water level of the treated water.
 そして、ステップS19にて、第1ドレン弁66及び第2ドレン弁67を開放することで、ドレンライン65による入口側室53からのケーシング51内の処理水の排出を可能とする。また、ステップS20にて、逆洗弁64を開放することで、第2給水ライン34の給水を洗浄水として出口側室54内に供給する。すると、逆洗ライン63から出口側室54内に供給された給水が図示しないノズルによりスクリーン52における出口側室54側の面に噴射されることで、スクリーン52における入口側室53側の面に付着している異物が除去される。そして、スクリーン52から除去された異物は、給水と共に入口側室53からドレンライン65に流れ込み、排水処理設備に排出されて処理される。 Then, in step S19, the first drain valve 66 and the second drain valve 67 are opened, so that drainage of the treated water in the casing 51 from the inlet side chamber 53 by the drain line 65 is enabled. Further, in step S20, by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed. Then, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 into the drain line 65 together with the water supply, and is discharged to the drainage treatment facility to be treated.
 ステップS21では、逆洗弁64を開放してから予め設定された所定時間が経過したかどうかを判定する。この所定時間とは、スクリーン52の洗浄時間であり、スクリーン52からほとんどの異物を除去可能な洗浄時間を予め実験等により確認しておく。ここで、逆洗弁64を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、逆洗弁64を開放してから所定時間が経過したと判定(Yes)されると、ステップS22に移行する。 In step S21, it is determined whether a predetermined time set in advance has passed since the backwash valve 64 was opened. The predetermined time is the cleaning time of the screen 52, and the cleaning time capable of removing most foreign matter from the screen 52 is confirmed in advance by experiment or the like. Here, if it is determined (No) that the predetermined time has not elapsed since the opening of the backwashing valve 64, this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process proceeds to step S22.
 制御装置73は、ステップS22にて、逆洗弁64を閉止し、ステップS23にて、第1ドレン弁66及び第2ドレン弁67を閉止し、ステップS24にて、ベント弁62を閉止する。そして、ステップS25にて、出口側室54と出口弁44の間に設けられ復水器13に接続された図示しないバランス弁を開放することにより、ケーシング51内の空気を除去して真空状態とする。その後、入口弁43を開放することによりケーシング51に復水が満たされ通水の準備がなされる。 The controller 73 closes the backwash valve 64 in step S22, closes the first drain valve 66 and the second drain valve 67 in step S23, and closes the vent valve 62 in step S24. Then, in step S25, a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13 is opened to remove the air in the casing 51 to make a vacuum state. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
 このように第1実施形態のストレーナの洗浄装置にあっては、出口側室54に接続されるベントライン61と、ベントライン61に設けられるベント弁62と、出口側室54に接続されて洗浄水を供給可能な逆洗ライン63と、逆洗ライン63に設けられる逆洗弁64と、入口側室53に接続されて異物を排出可能なドレンライン65と、ドレンライン65に設けられるドレン弁66,67と、ケーシング51の内部圧力を吸引ライン68の圧力より高く調整する差圧発生装置とを備えている。 As described above, in the strainer cleaning apparatus according to the first embodiment, the vent line 61 connected to the outlet side chamber 54, the vent valve 62 provided on the vent line 61, and the outlet side chamber 54 are connected to wash water. A backwash line 63 which can be supplied, a backwash valve 64 provided in the backwash line 63, a drain line 65 connected to the inlet side chamber 53 capable of discharging foreign substances, and a drain valve 66, 67 provided in the drain line 65 And a differential pressure generator for adjusting the internal pressure of the casing 51 higher than the pressure of the suction line 68.
 従って、ベント弁62により出口側室54を大気に開放し、差圧発生装置によりケーシング51の内部圧力を吸引ライン68の圧力より高くなるように調整すると、ケーシング51内の処理水が吸引ライン68に流れてケーシング51内の水位が低下する。その後、所定の水位になった時点で、真空弁69を閉止し、逆洗弁64を開放して洗浄水を逆洗ライン63から出口側室54に供給すると共にドレン弁66,67を開放すると、スクリーン52に付着していた異物が除去され、異物が入口側室53からドレンライン65に排出される。即ち、差圧発生装置によりケーシング51の内部圧力を吸引ライン68の圧力より高く調整することで、ケーシング51内の処理水を早期に吸引ライン68に排出することができ、ストレーナ14の洗浄処理時間を短縮して処理効率を向上することができる。また、ストレーナ14の洗浄処理時間を短縮することができることから、それぞれのストレーナ41,42の交互の洗浄回数を増やせば、ストレーナ14(41,42)は小型であっても対応できるので、製造コストを低減することができる。 Therefore, when the outlet side chamber 54 is opened to the atmosphere by the vent valve 62 and the internal pressure of the casing 51 is adjusted to be higher than the pressure of the suction line 68 by the differential pressure generator, the treated water in the casing 51 is It flows and the water level in casing 51 falls. Thereafter, when the water level reaches a predetermined level, the vacuum valve 69 is closed and the backwash valve 64 is opened to supply flush water from the backwash line 63 to the outlet side chamber 54 and open the drain valves 66 and 67, The foreign matter adhering to the screen 52 is removed, and the foreign matter is discharged from the inlet side chamber 53 to the drain line 65. That is, by adjusting the internal pressure of the casing 51 higher than the pressure of the suction line 68 by the differential pressure generator, the treated water in the casing 51 can be discharged to the suction line 68 at an early stage. Can be shortened to improve processing efficiency. Further, since the cleaning process time of the strainer 14 can be shortened, the strainer 14 (41, 42) can be coped with a small size by increasing the number of times of alternately cleaning the respective strainers 41, 42, so the manufacturing cost Can be reduced.
 第1実施形態のストレーナの洗浄装置では、差圧発生装置として、出口側室54に接続されるベントライン61と、ベントライン61に設けられるベント弁62と、吸引ライン68と、吸引ライン68に設けられる真空弁69とを設けている。従って、真空弁69を開放すると、吸引ライン68から出口側室54に吸引力が作用し、ケーシング51の内部圧力が吸引ライン68の圧力より高くなり、ケーシング51内の処理水を吸引ライン68に急速に流すことができ、ケーシング51内の水位を早期に低下させることができる。 In the strainer cleaning apparatus according to the first embodiment, as a differential pressure generator, a vent line 61 connected to the outlet side chamber 54, a vent valve 62 provided on the vent line 61, a suction line 68, and a suction line 68 are provided. And a vacuum valve 69. Therefore, when the vacuum valve 69 is opened, a suction force acts from the suction line 68 to the outlet side chamber 54, the internal pressure of the casing 51 becomes higher than the pressure of the suction line 68, and the treated water in the casing 51 is rapidly applied to the suction line 68. The water level in the casing 51 can be reduced early.
 第1実施形態のストレーナの洗浄装置では、第1給水ライン31は、真空圧状態に維持され、吸引ライン68を第1給水ライン31における入口弁43より上流側の入口ライン32aに接続している。従って、吸引ライン68を真空圧状態に維持された入口ライン32aに接続するだけで、ケーシング51内の処理水を吸引ライン68に流し、ケーシング51内の水位を早期に低下させることができる。 In the strainer cleaning apparatus according to the first embodiment, the first water supply line 31 is maintained at a vacuum pressure, and the suction line 68 is connected to the inlet line 32 a on the upstream side of the inlet valve 43 in the first water supply line 31. . Therefore, only by connecting the suction line 68 to the inlet line 32a maintained at the vacuum pressure, the treated water in the casing 51 can be flowed to the suction line 68, and the water level in the casing 51 can be lowered early.
 第1実施形態のストレーナの洗浄装置では、吸引ライン68をドレンライン65に接続し、ドレンライン65における吸引ライン68との接続部の上流側と下流側にそれぞれ第1ドレン弁66と第2ドレン弁67を設けている。従って、ケーシング51内の水位が低下した後、真空弁69を閉止した後、逆洗弁64を開放して洗浄水を逆洗ライン63から出口側室54に供給すると共に、第1ドレン弁66及び第2ドレン弁67を開放すると、スクリーン52に付着していた異物が入口側室53からドレンライン65に排出されると共に、吸引ライン68に残っている処理水も排出することができる。 In the strainer cleaning apparatus according to the first embodiment, the suction line 68 is connected to the drain line 65, and the first drain valve 66 and the second drain are connected upstream and downstream of a connection portion of the drain line 65 with the suction line 68, respectively. A valve 67 is provided. Therefore, after the water level in the casing 51 is lowered, the vacuum valve 69 is closed, and then the backwash valve 64 is opened to supply flush water from the backwash line 63 to the outlet side chamber 54 and the first drain valve 66 and When the second drain valve 67 is opened, the foreign matter adhering to the screen 52 is discharged from the inlet side chamber 53 to the drain line 65, and the treated water remaining in the suction line 68 can also be discharged.
 第1実施形態のストレーナの洗浄装置では、ケーシング51内の水位を検出または推定する水位検出推定装置と、ケーシング51内の水位が予め設定された所定水位まで低下すると、真空弁69を閉止すると共に逆洗弁64及びドレン弁66,67を開放する制御装置73とを設けている。従って、ケーシング51内の水位が所定水位まで低下すると、真空弁69を閉止すると共に逆洗弁64及びドレン弁66,67を開放するため、ケーシング51内の排水と異物除去を連続して実施することができる。 In the strainer cleaning apparatus according to the first embodiment, the water level detection / estimation device for detecting or estimating the water level in the casing 51 and the vacuum valve 69 are closed when the water level in the casing 51 falls to a predetermined water level set in advance. A controller 73 for opening the backwash valve 64 and the drain valves 66 and 67 is provided. Therefore, when the water level in the casing 51 drops to a predetermined water level, the drainage in the casing 51 and the removal of foreign matter are continuously performed in order to close the vacuum valve 69 and open the backwash valve 64 and the drain valves 66 and 67. be able to.
 また、第1実施形態のストレーナの洗浄方法にあっては、入口弁43と出口弁44を閉止する工程と、出口側室54を大気開放する工程と、ケーシング51の内部圧力を入口側室53に接続される吸引ライン68の圧力より高く調整する工程と、ケーシング51内の水位が予め設定された所定水位まで低下すると出口側室54に洗浄水を供給すると共にドレンライン65を開放する工程とを有している。 In the strainer cleaning method according to the first embodiment, the steps of closing the inlet valve 43 and the outlet valve 44, opening the outlet side chamber 54 to the atmosphere, and connecting the internal pressure of the casing 51 to the inlet side chamber 53 Adjusting the pressure higher than the pressure of the suction line 68, and supplying the cleaning water to the outlet side chamber 54 and opening the drain line 65 when the water level in the casing 51 falls to a predetermined level previously set. ing.
 従って、ケーシング51の内部圧力を出口側室54に接続される吸引ライン68の圧力より高く調整することで、ケーシング51内の処理水を早期に吸引ライン68に排出することができ、ストレーナ14(41,42)の洗浄処理時間を短縮して処理効率を向上することができる。 Therefore, by adjusting the internal pressure of the casing 51 higher than the pressure of the suction line 68 connected to the outlet side chamber 54, the treated water in the casing 51 can be discharged to the suction line 68 at an early stage. , 42) can be shortened to improve the processing efficiency.
 なお、上述した第1実施形態では、ケーシング51の内部の水位を検出する水位検出推定装置として、計測ライン70と水位計71と計測器側開閉弁72を設けたが、この構成に限定されるものではない。例えば、入口弁43と出口弁44を閉止し、ベント弁62と真空弁69を開放してから、ケーシング51内の水位が所定水位まで低下する時間を予め実験等により計測しておく。そして、制御装置73は、ベント弁62と真空弁69を開放してから所定時間が経過したら、真空弁69を閉止すると共に逆洗弁64及び各ドレン弁66,67を開放するようにしてもよい。 In the first embodiment described above, the measurement line 70, the water level gauge 71, and the measuring device side open / close valve 72 are provided as the water level detection / estimation device for detecting the water level inside the casing 51, but this configuration is limited It is not a thing. For example, after the inlet valve 43 and the outlet valve 44 are closed and the vent valve 62 and the vacuum valve 69 are opened, the time when the water level in the casing 51 falls to a predetermined water level is measured in advance by experiment or the like. Then, the control device 73 closes the vacuum valve 69 and opens the backwash valve 64 and the drain valves 66 and 67 when a predetermined time elapses after the vent valve 62 and the vacuum valve 69 are opened. Good.
[第2実施形態]
 図4は、第2実施形態のストレーナの洗浄装置を表す概略図、図5は、第2実施形態のストレーナの洗浄方法を表すフローチャートである。なお、上述した実施形態と同様の機能を有する部材には、同一の符号を付して詳細な説明は省略する。
Second Embodiment
FIG. 4 is a schematic view showing a strainer cleaning apparatus according to the second embodiment, and FIG. 5 is a flowchart showing a strainer cleaning method according to the second embodiment. The members having the same functions as those in the above-described embodiment are denoted by the same reference numerals, and detailed descriptions thereof will be omitted.
 第2実施形態において、図4に示すように、ケーシング51は、出口側室54にベントライン61が接続され、ベント弁62が設けられている。ケーシング51は、出口側室54に逆洗ライン63が接続され、逆洗弁64が設けられている。ケーシング51は、入口側室53にドレンライン65が接続され、ドレン弁66が設けられている。 In the second embodiment, as shown in FIG. 4, in the casing 51, the vent line 61 is connected to the outlet side chamber 54, and the vent valve 62 is provided. In the casing 51, a backwash line 63 is connected to the outlet side chamber 54, and a backwash valve 64 is provided. In the casing 51, a drain line 65 is connected to the inlet side chamber 53, and a drain valve 66 is provided.
 第1ストレーナ41は、ケーシング51の内部圧力をドレンライン65の圧力より高く調整する差圧発生装置が設けられている。差圧発生装置は、逆洗ライン63に接続される加圧ライン81と、加圧ライン81に設けられる加圧弁82及び加圧ポンプ(加圧装置)83とを有している。即ち、加圧ライン81は、一端部が逆洗ライン63における逆洗弁64より出口側室54側に接続され、加圧弁82と加圧ポンプ83が設けられている。この場合、加圧ライン81は、出口側室54に直接接続してもよいし、入口側室53に接続してもよい。また、ここでは、加圧装置として加圧ポンプ83を適用したが、プラント内に加圧エアラインがあれば、加圧ライン81をこの加圧エアラインに接続してもよい。 The first strainer 41 is provided with a differential pressure generator that adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65. The differential pressure generator has a pressure line 81 connected to the backwash line 63, and a pressure valve 82 and a pressure pump (pressure device) 83 provided on the pressure line 81. That is, one end of the pressurizing line 81 is connected to the outlet side chamber 54 side of the backwashing valve 64 in the backwashing line 63, and the pressurizing valve 82 and the pressurizing pump 83 are provided. In this case, the pressure line 81 may be directly connected to the outlet side chamber 54 or may be connected to the inlet side chamber 53. Moreover, although the pressurization pump 83 was applied as a pressurization apparatus here, if there exists a pressurization air line in a plant, you may connect the pressurization line 81 to this pressurization air line.
 そのため、加圧弁82を開放して加圧ポンプ83を駆動すると、加圧空気が加圧ライン81及び逆洗ライン63を通して出口側室54に供給される。すると、ベント弁62は閉止されているので、ケーシング51(出口側室54)は、加圧ライン81から加圧空気が供給されることで、ケーシング51の内部圧力がドレンライン65の圧力より高くなる。 Therefore, when the pressurizing valve 82 is opened and the pressurizing pump 83 is driven, pressurized air is supplied to the outlet side chamber 54 through the pressurizing line 81 and the backwash line 63. Then, since the vent valve 62 is closed, the internal pressure of the casing 51 becomes higher than the pressure of the drain line 65 by the pressurized air being supplied from the pressurizing line 81 to the casing 51 (the outlet side chamber 54) .
 制御装置73は、入口弁43、出口弁44、ベント弁62、逆洗弁64、ドレン弁66、加圧弁82に接続されていると共に、外部の操作装置(図示略)からの制御信号が入力可能となっている。制御装置73は、操作装置からの制御信号に応じて入口弁43、出口弁44、ベント弁62、逆洗弁64、ドレン弁66、加圧弁82を開閉制御可能となっている。 The control device 73 is connected to the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82, and receives control signals from an external operating device (not shown). It is possible. The controller 73 can control the opening and closing of the inlet valve 43, the outlet valve 44, the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82 in accordance with a control signal from the operating device.
 ここで、第2実施形態のストレーナの洗浄装置による第1ストレーナ41の洗浄方法について説明する。なお、ストレーナの使用状態、即ち、通水状態では、ベント弁62、逆洗弁64、ドレン弁66、加圧弁82は閉止状態である。 Here, a method of cleaning the first strainer 41 by the apparatus for cleaning a strainer of the second embodiment will be described. In the use state of the strainer, that is, in the water flowing state, the vent valve 62, the backwash valve 64, the drain valve 66, and the pressurizing valve 82 are closed.
 第2実施形態のストレーナの洗浄方法において、図3及び図5に示すように、ステップS31にて、待機側の第2ストレーナ42の入口弁45及び出口弁46を開放して第2ストレーナ42に通水し、ステップS32にて、清掃側(使用中)の第1ストレーナ41の入口弁43及び出口弁44を閉止して第1ストレーナ41への通水を停止する。 In the method of cleaning the strainer according to the second embodiment, as shown in FIGS. 3 and 5, in step S31, the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to the second strainer 42. Water is supplied, and in step S32, the inlet valve 43 and the outlet valve 44 of the first strainer 41 on the cleaning side (in use) are closed to stop the water supply to the first strainer 41.
 ステップS33にて、ドレン弁66を開放することで、ドレンライン65による入口側室53からのケーシング51内の処理水の排出を可能とする。そして、ステップS34にて、加圧弁82を開放すると共に加圧ポンプ83を駆動して加圧ライン81及び逆洗ライン63により出口側室54に加圧空気を供給する。すると、ケーシング51の出口側室54の圧力がドレンライン65の圧力より相対的に高くなる。そのため、ケーシング51内の処理水が入口側室53からドレンライン65により排出されることで、ケーシング51内の水位が減少する。 In step S33, the drain valve 66 is opened to allow the drain line 65 to discharge the treated water in the casing 51 from the inlet side chamber 53. Then, in step S34, the pressurizing valve 82 is opened and the pressurizing pump 83 is driven to supply pressurized air to the outlet side chamber 54 through the pressurizing line 81 and the backwash line 63. Then, the pressure in the outlet side chamber 54 of the casing 51 becomes relatively higher than the pressure in the drain line 65. Therefore, when the treated water in the casing 51 is discharged from the inlet side chamber 53 by the drain line 65, the water level in the casing 51 decreases.
 ステップS35にて、加圧弁82を開放してから予め設定された所定時間が経過したかどうかを判定する。この所定時間とは、ケーシング51内の処理水が排出される排出時間であり、予め実験等により確認しておく。ここで、加圧弁82を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、加圧弁82を開放してから所定時間が経過したと判定(Yes)されると、ステップS36に移行する。ステップS36では、加圧弁82を閉止すると共に加圧ポンプ83の駆動を停止する。 In step S35, it is determined whether or not a predetermined time set in advance has elapsed since the pressurizing valve 82 was opened. The predetermined time is a discharge time during which the treated water in the casing 51 is discharged, and is previously confirmed by an experiment or the like. Here, if it is determined that the predetermined time has not elapsed since the pressurization valve 82 was opened (No), this process is continued, and it is determined that the predetermined time has elapsed since the pressurization valve 82 was opened (Yes) Then, the process proceeds to step S36. In step S36, the pressurizing valve 82 is closed and the driving of the pressurizing pump 83 is stopped.
 そして、ステップS37にて、逆洗弁64を開放することで、第2給水ライン34の給水を洗浄水として出口側室54内に供給する。すると、逆洗ライン63から出口側室54内に供給された給水が図示しないノズルによりスクリーン52における出口側室54側の面に噴射されることで、スクリーン52における入口側室53側の面に付着している異物が除去される。 Then, in step S37, by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed.
 ステップS38では、逆洗弁64を開放してから予め設定された所定時間(洗浄時間)が経過したかどうかを判定する。ここで、逆洗弁64を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、逆洗弁64を開放してから所定時間が経過したと判定(Yes)されると、ステップS39に移行する。制御装置73は、ステップS39にて、逆洗弁64を閉止し、ステップS40にて、ベント弁62を開放する。これにより、スクリーン52から除去された異物は、洗浄水と共に入口側室53からドレンライン65に流れ込み、排水処理設備に排出されて処理される。次いで、ステップS41にて、ベント弁62の開放時間が異物と給水を排出するのに適切な予め設定した所定時間が経過したかどうかを判定する。ベント弁62を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、所定時間が経過したと判定(Yes)されると、ステップS42にてベント弁62を閉止し、ステップS43にて、ドレン弁66を閉止する。そして、ステップS44にて、出口側室54と出口弁44の間に設けられ復水器13に接続された図示しないバランス弁を開放することにより、ケーシング51内の空気を除去して真空状態とする。その後、入口弁43を開放することによりケーシング51に復水が満たされ通水の準備がなされる。 In step S38, it is determined whether or not a predetermined time (washing time) set in advance has passed after the backwashing valve 64 is opened. Here, if it is determined (No) that the predetermined time has not elapsed since the opening of the backwashing valve 64, this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process moves to step S39. The controller 73 closes the backwash valve 64 in step S39, and opens the vent valve 62 in step S40. Thereby, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 to the drain line 65 together with the washing water, and is discharged to the drainage treatment facility to be treated. Next, in step S41, it is determined whether or not the opening time of the vent valve 62 has passed a preset predetermined time suitable for discharging the foreign matter and the water supply. If it is determined (No) that the predetermined time has not elapsed since the vent valve 62 was opened, this process is continued, and if it is determined (Yes) that the predetermined time has elapsed, the vent valve 62 is determined in step S42. Is closed, and the drain valve 66 is closed in step S43. Then, in step S44, a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13 is opened to remove the air in the casing 51 to make it into a vacuum state. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
 このように第2施形態のストレーナの洗浄装置にあっては、差圧発生装置として、出口側室54に接続される加圧ライン81と、加圧ライン81に設けられる加圧弁82とを設けている。 As described above, in the strainer cleaning apparatus according to the second embodiment, the pressure line 81 connected to the outlet side chamber 54 and the pressure valve 82 provided on the pressure line 81 are provided as a differential pressure generator. There is.
 従って、ドレン弁66によりドレンライン65を開放した状態で、加圧弁82を開放すると、ケーシング51内に加圧空気が供給されることでケーシング51の内部圧力がドレンライン65の圧力より高くなり、ケーシング51内の処理水がドレンライン65に流れてケーシング51内の水位が低下する。ここで、逆洗弁64を開放して洗浄水を逆洗ライン63から出口側室54に供給すると、スクリーン52に付着していた異物が除去され、異物が入口側室53からドレンライン65に排出される。即ち、加圧ライン81からの加圧空気によりケーシング51の内部圧力をドレンライン65の圧力より高く調整することで、ケーシング51内の処理水を早期にドレンライン65に排出することができ、ストレーナ14の洗浄処理時間を短縮して処理効率を向上することができる。また、出口側室54に加圧ライン81を接続するだけでケーシング51内の水位を早期に低下させることができる。 Therefore, when the pressurizing valve 82 is opened in a state where the drain line 65 is opened by the drain valve 66, the internal pressure of the casing 51 becomes higher than the pressure of the drain line 65 by supplying pressurized air into the casing 51, The treated water in the casing 51 flows to the drain line 65, and the water level in the casing 51 decreases. Here, when the backwashing valve 64 is opened and washing water is supplied from the backwashing line 63 to the outlet side chamber 54, the foreign matter adhering to the screen 52 is removed, and the foreign matter is discharged from the inlet side chamber 53 to the drain line 65. Ru. That is, by adjusting the internal pressure of the casing 51 higher than the pressure of the drain line 65 by the pressurized air from the pressurizing line 81, the treated water in the casing 51 can be discharged to the drain line 65 at an early stage, and the strainer The processing time can be improved by shortening the cleaning process time of 14. Further, the water level in the casing 51 can be reduced early by only connecting the pressure line 81 to the outlet side chamber 54.
 第2実施形態のストレーナの洗浄装置では、加圧ライン81に加圧装置としての加圧ポンプ83を設けている。従って、加圧ライン81に加圧ポンプ83を設けるだけで、ケーシング51内の処理水をドレンライン65に流し、ケーシング51内の水位を早期に低下させることができる。 In the strainer cleaning apparatus according to the second embodiment, the pressure line 81 is provided with a pressure pump 83 as a pressure device. Therefore, only by providing the pressurizing pump 83 in the pressurizing line 81, the treated water in the casing 51 can be flowed to the drain line 65, and the water level in the casing 51 can be reduced early.
[第3実施形態]
 図6は、第3実施形態のストレーナの洗浄装置を表す概略図、図7は、第3実施形態のストレーナの洗浄方法を表すフローチャートである。なお、上述した実施形態と同様の機能を有する部材には、同一の符号を付して詳細な説明は省略する。
Third Embodiment
FIG. 6 is a schematic view showing a strainer cleaning apparatus according to the third embodiment, and FIG. 7 is a flowchart showing a strainer cleaning method according to the third embodiment. The members having the same functions as those in the above-described embodiment are denoted by the same reference numerals, and detailed descriptions thereof will be omitted.
 第3実施形態において、図6に示すように、ケーシング51は、出口側室54にベントライン61が接続され、ベントライン61にベント弁62が設けられている。ケーシング51は、出口側室54に逆洗ライン63が接続され、逆洗ライン63に逆洗弁64が設けられている。ケーシング51は、入口側室53にドレンライン65が接続され、ドレンライン65に第1ドレン弁66と第2ドレン弁67が直列に設けられている。 In the third embodiment, as shown in FIG. 6, in the casing 51, a vent line 61 is connected to the outlet side chamber 54, and a vent valve 62 is provided in the vent line 61. In the casing 51, the backwash line 63 is connected to the outlet side chamber 54, and the backwash line 63 is provided with a backwash valve 64. In the casing 51, a drain line 65 is connected to the inlet side chamber 53, and a first drain valve 66 and a second drain valve 67 are provided in series in the drain line 65.
 第1ストレーナ41は、ケーシング51の内部圧力をドレンライン65の圧力より高く調整する差圧発生装置が設けられている。差圧発生装置は、逆洗ライン63に接続される加圧ライン81と、加圧ライン81に設けられる加圧弁82及び加圧ポンプ83とを有している。また、差圧発生装置は、ケーシング51の出口側室54に接続される吸引ライン68と、吸引ライン68に設けられる真空弁69とを有している。 The first strainer 41 is provided with a differential pressure generator that adjusts the internal pressure of the casing 51 higher than the pressure of the drain line 65. The differential pressure generator has a pressure line 81 connected to the backwash line 63 and a pressure valve 82 and a pressure pump 83 provided on the pressure line 81. Further, the differential pressure generator has a suction line 68 connected to the outlet side chamber 54 of the casing 51 and a vacuum valve 69 provided in the suction line 68.
 ここで、第3実施形態のストレーナの洗浄装置による第1ストレーナ41の洗浄方法について説明する。なお、ストレーナの使用状態、即ち、通水状態では、ベント弁62、逆洗弁64、第1ドレン弁66、第2ドレン弁67、真空弁69、計測器側開閉弁72、加圧弁82は閉止状態である。 Here, a method of cleaning the first strainer 41 by the apparatus for cleaning a strainer of the third embodiment will be described. In the use state of the strainer, that is, in the water flowing state, the vent valve 62, the backwash valve 64, the first drain valve 66, the second drain valve 67, the vacuum valve 69, the measuring instrument side on-off valve 72, and the pressurizing valve 82 It is closed.
 第3実施形態のストレーナの洗浄方法において、図3及び図7に示すように、ステップS51にて、待機側の第2ストレーナ42の入口弁45及び出口弁46を開放して第2ストレーナ42に通水し、ステップS52にて、清掃側(使用中)の第1ストレーナ41の入口弁43及び出口弁44を閉止して第1ストレーナ41への通水を停止する。 In the method of cleaning the strainer according to the third embodiment, as shown in FIGS. 3 and 7, in step S 51, the inlet valve 45 and the outlet valve 46 of the second strainer 42 on the standby side are opened to the second strainer 42. Water is supplied, and in step S52, the inlet valve 43 and the outlet valve 44 of the first strainer 41 on the cleaning side (in use) are closed to stop the water supply to the first strainer 41.
 ステップS53にて、加圧弁82を開放すると共に加圧ポンプ83を駆動して加圧ライン81及び逆洗ライン63により出口側室54に加圧空気を供給する。また、ステップS54にて、計測器側開閉弁72を開放してケーシング51(出口側室54)と水位計71を連通し、水位計71によりケーシング51内の処理水の水位を計測可能とする。そして、ステップS55にて、真空弁69を開放して吸引ライン68により出口側室54と入口ライン32aとを連通する。 In step S53, the pressurizing valve 82 is opened and the pressurizing pump 83 is driven to supply pressurized air to the outlet side chamber 54 through the pressurizing line 81 and the backwash line 63. Further, in step S54, the measuring instrument side open / close valve 72 is opened to communicate the casing 51 (outlet side chamber 54) with the water level gauge 71, and the water level gauge 71 can measure the water level of the treated water. Then, in step S55, the vacuum valve 69 is opened, and the outlet side chamber 54 and the inlet line 32a are communicated by the suction line 68.
 すると、出口側室54に加圧空気が供給されることで、ケーシング51の出口側室54の圧力が高くなる。また、入口ライン32aの真空度が吸引ライン68を通して出口側室54に作用することでも、ケーシング51の出口側室54の圧力が高くなる。その結果、ケーシング51の出口側室54の圧力が吸引ライン68の圧力より相対的に高くなる。そのため、出口側室54内の処理水が吸引ライン68から入口ライン32aに流れることで、ケーシング51内の水位が急速に減少する。 Then, the pressurized air is supplied to the outlet side chamber 54, whereby the pressure in the outlet side chamber 54 of the casing 51 becomes high. In addition, the pressure of the outlet side chamber 54 of the casing 51 is also increased by the degree of vacuum of the inlet line 32 a acting on the outlet side chamber 54 through the suction line 68. As a result, the pressure in the outlet side chamber 54 of the casing 51 becomes relatively higher than the pressure in the suction line 68. Therefore, when the treated water in the outlet side chamber 54 flows from the suction line 68 to the inlet line 32a, the water level in the casing 51 is rapidly reduced.
 制御装置73は、ステップS56にて、ケーシング51内の水位が所定水位レベルまで低下したかどうかを判定している。ここで、ケーシング51内の水位が所定水位レベルまで低下していないと判定(No)すると、この処理を継続し、ケーシング51内の水位が所定水位レベルまで低下したと判定(Yes)すると、ステップS57に移行する。ステップS57では、加圧弁82を閉止すると共に加圧ポンプ83の駆動を停止する。また、ステップS58では、真空弁69を閉止して吸引ライン68による出口側室54と入口ライン32aとの連通を遮断し、ステップS59では、計測器側開閉弁72を閉止して水位計71によるケーシング51内の処理水の水位の計測を停止する。 At step S56, control device 73 determines whether the water level in casing 51 has dropped to a predetermined water level. Here, if it is determined that the water level in casing 51 has not dropped to the predetermined water level (No), this process is continued, and if it is determined that the water level in casing 51 has dropped to the predetermined water level (Yes), step Transfer to S57. In step S57, the pressurizing valve 82 is closed and the driving of the pressurizing pump 83 is stopped. Further, in step S58, the vacuum valve 69 is closed to shut off the communication between the outlet side chamber 54 and the inlet line 32a by the suction line 68, and in step S59, the measuring device side on-off valve 72 is closed. Stop measuring the level of treated water in 51.
 そして、ステップS60にて、第1ドレン弁66及び第2ドレン弁67を開放することで、ドレンライン65による入口側室53からのケーシング51内の処理水の排出を可能とする。また、ステップS61にて、逆洗弁64を開放することで、第2給水ライン34の給水を洗浄水として出口側室54内に供給する。すると、逆洗ライン63から出口側室54内に供給された給水が図示しないノズルによりスクリーン52における出口側室54側の面に噴射されることで、スクリーン52における入口側室53側の面に付着している異物が除去される。 Then, in step S60, the first drain valve 66 and the second drain valve 67 are opened to allow the drain line 65 to discharge the treated water in the casing 51 from the inlet side chamber 53. Further, in step S61, by opening the backwash valve 64, the water supply of the second water supply line 34 is supplied as wash water into the outlet side chamber 54. Then, the water supplied from the backwash line 63 into the outlet side chamber 54 is sprayed to the surface on the outlet side chamber 54 side of the screen 52 by a nozzle not shown, and adheres to the surface on the inlet side chamber 53 side in the screen 52 Foreign substances are removed.
 ステップS62では、逆洗弁64を開放してから予め設定された所定時間が経過したかどうかを判定する。ここで、逆洗弁64を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、逆洗弁64を開放してから所定時間が経過したと判定(Yes)されると、ステップS63に移行する。制御装置73は、ステップS63にて、逆洗弁64を閉止し、ステップS64にてベント弁62を開放する。これにより、スクリーン52から除去された異物は、洗浄水と共に入口側室53からドレンライン65に流れ込み、排水処理設備に排出されて処理される。次いで、ステップS65にて、ベント弁62の開放時間が異物と給水を排出するのに適切な予め設定した所定時間が経過したかどうかを判定する。ベント弁62を開放してから所定時間が経過していないと判定(No)されるとこの処理を継続し、所定時間が経過したと判定(Yes)されると、ステップS66にてベント弁62を閉止し、ステップS67にて、第1ドレン弁66及び第2ドレン弁67を閉止する。そして、ステップS68にて、出口側室54と出口弁44の間に設けられ復水器13に接続された図示しないバランス弁を開放することにより、ケーシング51内の空気を除去して真空状態とする。その後、入口弁43を開放することによりケーシング51に復水が満たされ通水の準備がなされる。 In step S62, it is determined whether a predetermined time set in advance has passed since the backwash valve 64 was opened. Here, if it is determined (No) that the predetermined time has not elapsed since the opening of the backwashing valve 64, this process is continued, and it is determined that the predetermined time has elapsed since the opening of the backwashing valve 64 ( If yes, the process moves to step S63. The control device 73 closes the backwash valve 64 in step S63, and opens the vent valve 62 in step S64. Thereby, the foreign matter removed from the screen 52 flows from the inlet side chamber 53 to the drain line 65 together with the washing water, and is discharged to the drainage treatment facility to be treated. Next, in step S65, it is determined whether the opening time of the vent valve 62 has passed a predetermined time set in advance that is appropriate for discharging the foreign matter and the water supply. If it is determined (No) that the predetermined time has not elapsed since the vent valve 62 was opened, this process is continued, and if it is determined (Yes) that the predetermined time has elapsed, the vent valve 62 is determined in step S66. Are closed, and the first drain valve 66 and the second drain valve 67 are closed in step S67. Then, in step S68, the air in the casing 51 is removed to be in a vacuum state by opening a balance valve (not shown) provided between the outlet side chamber 54 and the outlet valve 44 and connected to the condenser 13. . Thereafter, by opening the inlet valve 43, the casing 51 is filled with condensed water and preparation for water passage is made.
 このように第3施形態のストレーナの洗浄装置にあっては、差圧発生装置として、出口側室54に接続される吸引ライン68と、吸引ライン68に設けられる真空弁69とを設けると共に、出口側室54に接続される加圧ライン81と、加圧ライン81に設けられる加圧弁82とを設けている。 As described above, in the strainer cleaning apparatus according to the third embodiment, the suction line 68 connected to the outlet side chamber 54 and the vacuum valve 69 provided on the suction line 68 are provided as a differential pressure generating device, and the outlet A pressure line 81 connected to the side chamber 54 and a pressure valve 82 provided on the pressure line 81 are provided.
 従って、加圧ライン81からの加圧空気と、吸引ライン68による吸引力によりケーシング51の内部圧力を吸引ライン68の圧力より高く調整することで、ケーシング51内の処理水を早期に吸引ラインに排出することができ、ストレーナ14の洗浄処理時間を短縮して処理効率を向上することができる。 Therefore, by adjusting the internal pressure of the casing 51 higher than the pressure of the suction line 68 by the pressurized air from the pressure line 81 and the suction force of the suction line 68, the treated water in the casing 51 can be made into the suction line early. It is possible to discharge and shorten the cleaning processing time of the strainer 14 to improve the processing efficiency.
 なお、上述した第2、第3実施形態では、逆洗弁64を閉止したのちにベント弁62を所定時間開放するように構成したが、加圧弁82を閉止後、逆洗弁64を開放する前にベント弁62を開放し、逆洗弁64を閉止した後、所定時間経過後にベント弁62を閉止するようにしてもよい。この構成によれば、ベント弁62の開放時間をより短くすることが可能となる。 In the second and third embodiments described above, the vent valve 62 is opened for a predetermined time after the backwash valve 64 is closed, but the backwash valve 64 is opened after the pressurizing valve 82 is closed. The vent valve 62 may be closed after a predetermined time has elapsed after the vent valve 62 has been opened and the backwash valve 64 has been closed. According to this configuration, the opening time of the vent valve 62 can be further shortened.
 また、上述した第2、第3実施形態では、逆洗ライン63による洗浄で生じた異物と洗浄水の排出のために、ベント弁62を開放し、ドレンライン65から排出するようにしたが、ベントライン61及びベント弁62を設けずに、逆洗ライン63による洗浄後、すなわち逆洗弁64を閉止後に、加圧弁82を開放し、加圧ライン81による圧力により、ドレンライン65から異物と洗浄水を排出するようにしてもよい。これにより、ベントライン61による排出よりも、より早く異物と洗浄水を排出することが可能となる。 Further, in the second and third embodiments described above, the vent valve 62 is opened and drained from the drain line 65 in order to drain out the foreign matter and flush water generated by the backwash line 63. After cleaning by the backwash line 63 without providing the vent line 61 and the vent valve 62, that is, after closing the backwash valve 64, the pressure valve 82 is opened, and pressure from the pressure line 81 causes foreign matter The washing water may be discharged. As a result, it is possible to discharge the foreign matter and the washing water more quickly than the discharge by the vent line 61.
 また、上述した第1~第3実施形態では、制御装置73によって自動制御するよう構成したが、手動操作によって実施してもよい。 Further, in the above-described first to third embodiments, automatic control is performed by the control device 73. However, manual control may be performed.
 また、上述した第1~第3実施形態では、復水器13に接続される第1給水ライン31を2つの分岐ライン32,33に分岐し、分岐ライン32に入口弁43と第1ストレーナ41と出口弁44を設け、分岐ライン33に入口弁45と第2ストレーナ42と出口弁46を設けたが、この分岐数は2つに限らず3つ以上としてもよい。 In the first to third embodiments described above, the first water supply line 31 connected to the condenser 13 is branched into two branch lines 32 and 33, and the inlet valve 43 and the first strainer 41 are connected to the branch line 32. The outlet valve 44 is provided, and the inlet valve 45, the second strainer 42, and the outlet valve 46 are provided in the branch line 33. However, the number of branches is not limited to two and may be three or more.
 また、上述した第1~第3実施形態では、本発明のストレーナの洗浄装置及び方法を火力発電プラントの給水系統に適用して説明したが、原子力発電プラントや地熱発電プラントの給水系統、または、その他の給水系統に適用することもできる。 In the first to third embodiments described above, the strainer cleaning apparatus and method of the present invention have been described as applied to the water supply system of a thermal power plant, but the water supply system of a nuclear power plant or a geothermal power plant, or It can also be applied to other water supply systems.
 10 火力発電プラント
 11 ボイラ
 12 蒸気タービン
 13 復水器
 14 ストレーナ
 15 復水ポンプ
 16 低圧給水加熱器
 17 脱気器
 18 高圧給水加熱器
 19 発電機
 31 第1給水ライン
 32,33 分岐ライン
 32a 入口ライン
 32b 出口ライン
 34 第2給水ライン
 41 第1ストレーナ
 42 第2ストレーナ
 43,45 入口弁
 44,46 出口弁
 51 ケーシング
 52 スクリーン(メッシュ)
 53 入口側室
 54 出口側室
 61 ベントライン
 62 ベント弁
 63 逆洗ライン
 64 逆洗弁
 65 ドレンライン
 66 第1ドレン弁
 67 第2ドレン弁
 68 吸引ライン(差圧発生装置)
 69 真空弁(吸引弁、差圧発生装置)
 70 計測ライン
 71 水位計
 72 計測器側開閉弁
 73 制御装置
 81 加圧ライン(差圧発生装置)
 82 加圧弁(差圧発生装置)
 83 加圧ポンプ(差圧発生装置、加圧装置)
DESCRIPTION OF SYMBOLS 10 thermal power generation plant 11 boiler 12 steam turbine 13 condenser 14 strainer 15 condensate pump 16 low pressure feed water heater 17 deaerator 18 high pressure feed water heater 19 generator 31 1st feed line 32, 33 branch line 32a inlet line 32b Outlet line 34 second water supply line 41 first strainer 42 second strainer 43, 45 inlet valve 44, 46 outlet valve 51 casing 52 screen (mesh)
53 inlet side chamber 54 outlet side chamber 61 vent line 62 vent valve 63 backwash line 64 backwash valve 65 drain line 66 first drain valve 67 second drain valve 68 suction line (differential pressure generator)
69 Vacuum valve (suction valve, differential pressure generator)
70 Measurement line 71 Water level gauge 72 Measuring device side open / close valve 73 Control device 81 Pressurization line (differential pressure generator)
82 Pressure valve (differential pressure generator)
83 Pressure pump (differential pressure generator, pressure device)

Claims (14)

  1.  ケーシングの内部がスクリーンにより入口側室と出口側室に区画され、前記入口側室に給水ラインが接続されて入口弁が設けられる一方、前記出口側室に給水ラインが接続されて出口弁が設けられるストレーナにおいて、
     前記出口側室に接続されて洗浄水を供給可能な逆洗ラインと、
     前記逆洗ラインに設けられる逆洗弁と、
     前記入口側室のドレン排出側に接続されて異物を排出可能なドレンラインと、
     前記ドレンラインに設けられるドレン弁と、
     前記ケーシングの内部圧力を前記ケーシングのドレン排出側の圧力より高く調整する差圧発生装置と、
     を備えることを特徴とするストレーナの洗浄装置。
    In a strainer in which the interior of the casing is partitioned by a screen into an inlet side chamber and an outlet side chamber, a water supply line is connected to the inlet side chamber to provide an inlet valve, and a water supply line is connected to the outlet side chamber to provide an outlet valve;
    A backwash line connected to the outlet side chamber and capable of supplying washing water;
    A backwash valve provided in the backwash line;
    A drain line connected to the drain discharge side of the inlet side chamber for discharging foreign substances;
    A drain valve provided in the drain line;
    A differential pressure generator for adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing;
    An apparatus for cleaning a strainer, comprising:
  2.  前記差圧発生装置は、前記出口側室に接続されるベントラインと、前記ベントラインに設けられるベント弁と、前記出口側室のドレン排出側に接続される吸引ラインと、前記吸引ラインに設けられる吸引弁とを有することを特徴とする請求項1に記載のストレーナの洗浄装置。 The differential pressure generator includes a vent line connected to the outlet side chamber, a vent valve provided on the vent line, a suction line connected to the drain discharge side of the outlet side chamber, and suction provided on the suction line. The strainer cleaning apparatus according to claim 1, further comprising a valve.
  3.  前記給水ラインは、真空圧状態に維持され、前記吸引ラインは、前記給水ラインにおける前記入口弁より上流側に接続され、前記吸引ラインの内部圧力より前記ケーシングの内部圧力を高くすることを特徴とする請求項2に記載のストレーナの洗浄装置。 The water supply line is maintained at a vacuum pressure, and the suction line is connected upstream of the inlet valve in the water supply line, and the internal pressure of the casing is made higher than the internal pressure of the suction line. The strainer cleaning device according to claim 2.
  4.  前記吸引ラインは、前記ドレンラインに接続され、前記ドレンラインにおける前記吸引ラインとの接続部の上流側と下流側にそれぞれ前記ドレン弁として第1ドレン弁と第2ドレン弁が設けられることを特徴とする請求項3に記載のストレーナの洗浄装置。 The suction line is connected to the drain line, and a first drain valve and a second drain valve are respectively provided as the drain valve on the upstream side and the downstream side of the connection portion of the drain line with the suction line. The strainer cleaning apparatus according to claim 3, wherein
  5.  前記ケーシング内の水位を検出または推定する水位検出推定装置が設けられることを特徴とする請求項3または請求項4に記載のストレーナの洗浄装置。 5. The strainer cleaning device according to claim 3, further comprising a water level detection and estimation device that detects or estimates the water level in the casing.
  6.  前記ケーシング内の水位を検出または推定する水位検出推定装置と、前記ケーシング内の水位が予め設定された所定水位まで低下すると前記吸引弁を閉止すると共に前記逆洗弁及び前記ドレン弁を開放する制御装置とが設けられることを特徴とする請求項3または請求項4に記載のストレーナの洗浄装置。 A water level detection and estimation device for detecting or estimating the water level in the casing, and a control for closing the suction valve and opening the backwash valve and the drain valve when the water level in the casing falls to a predetermined water level set in advance The strainer cleaning apparatus according to claim 3 or 4, wherein an apparatus is provided.
  7.  前記差圧発生装置は、前記入口側室または前記出口側室に接続される加圧ラインと、前記加圧ラインに設けられる加圧弁とを有することを特徴とする請求項1に記載のストレーナの洗浄装置。 The strainer cleaning device according to claim 1, wherein the differential pressure generating device includes a pressurizing line connected to the inlet side chamber or the outlet side chamber, and a pressurizing valve provided to the pressurizing line. .
  8.  前記加圧ラインは、加圧装置に接続され、前記ドレンラインの圧力より前記ケーシングの内部圧力を高くすることを特徴とする請求項7に記載のストレーナの洗浄装置。 The strainer cleaning apparatus according to claim 7, wherein the pressure line is connected to a pressure device, and the internal pressure of the casing is higher than the pressure of the drain line.
  9.  前記差圧発生装置は、前記加圧ラインが加圧装置に接続され、前記出口側室のドレン排出側に接続される吸引ラインと、前記吸引ラインに設けられる吸引弁とを有し、前記吸引ラインの圧力より前記ケーシングの内部圧力を高くすることを特徴とする請求項7に記載のストレーナの洗浄装置。 The differential pressure generator has a suction line connected to the drain side of the outlet chamber and the suction line connected to the pressure device, and a suction valve provided on the suction line, the suction line 8. The strainer cleaning apparatus according to claim 7, wherein the internal pressure of the casing is made higher than the pressure of.
  10.  前記給水ラインは、真空圧状態に維持され、前記吸引ラインは、前記給水ラインにおける前記入口弁より上流側に接続されることを特徴とする請求項9に記載のストレーナの洗浄装置。 The strainer cleaning apparatus according to claim 9, wherein the water supply line is maintained at a vacuum pressure, and the suction line is connected upstream of the inlet valve in the water supply line.
  11.  前記吸引ラインは、前記ドレンラインに接続され、前記ドレンラインにおける前記吸引ラインとの接続部の上流側と下流側にそれぞれ前記ドレン弁として第1ドレン弁と第2ドレン弁が設けられることを特徴とする請求項10に記載のストレーナの洗浄装置。 The suction line is connected to the drain line, and a first drain valve and a second drain valve are respectively provided as the drain valve on the upstream side and the downstream side of the connection portion of the drain line with the suction line. 11. The strainer cleaning apparatus according to claim 10, wherein
  12.  前記ケーシング内の水位を検出または推定する水位検出推定装置が設けられることを特徴とする請求項9から請求項11のいずれか一項に記載のストレーナの洗浄装置。 The strainer washing apparatus according to any one of claims 9 to 11, further comprising a water level detection and estimation device that detects or estimates the water level in the casing.
  13.  前記ケーシング内の水位が予め設定された所定水位まで低下すると前記吸引弁を閉止すると共に前記逆洗弁及び前記ドレン弁を開放する制御装置とが設けられることを特徴とする請求項12に記載のストレーナの洗浄装置。 13. The control device according to claim 12, further comprising: a controller that closes the suction valve and opens the backwash valve and the drain valve when the water level in the casing falls to a predetermined water level set in advance. Strainer cleaning device.
  14.  ケーシングの内部がスクリーンにより入口側室と出口側室に区画され、前記入口側室に給水ラインが接続されて入口弁が設けられる一方、前記出口側室に前記給水ラインが接続されて出口弁が設けられるストレーナにおいて、
     前記入口弁と前記出口弁を閉止する工程と、
     前記ケーシングの内部圧力を前記ケーシングのドレン排出側の圧力より高く調整する工程と、
     前記ケーシング内の水位が予め設定された所定水位まで低下すると前記出口側室に洗浄水を供給すると共にドレンラインを開放する工程と、
     を有することを特徴とするストレーナの洗浄方法。
    The inside of the casing is divided by a screen into an inlet side chamber and an outlet side chamber, a water supply line is connected to the inlet side chamber to provide an inlet valve, and a strainer is connected to the outlet side chamber and the water supply line is connected to provide an outlet valve. ,
    Closing the inlet valve and the outlet valve;
    Adjusting the internal pressure of the casing higher than the pressure on the drain discharge side of the casing;
    Supplying flush water to the outlet side chamber and opening the drain line when the water level in the casing falls to a predetermined level previously set;
    A method of cleaning a strainer, comprising:
PCT/JP2017/034009 2016-10-04 2017-09-21 Strainer cleaning device and method WO2018066366A1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627191A (en) * 2019-09-06 2019-12-31 中信环境技术(广州)有限公司 Pretreatment solid-liquid separation device and method
CN111167771A (en) * 2020-02-17 2020-05-19 青岛诺诚化学品安全科技有限公司 Online closed cleaning and detecting system and technological method for flame arrester

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110734125B (en) * 2019-11-12 2024-05-28 广东玮霖环保科技有限公司 Water level adjustable efficient filter tank back flushing method and structure
KR20230134553A (en) 2021-03-10 2023-09-21 미츠비시 파워 가부시키가이샤 Capture device, condensate equipment, and capture method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5551412A (en) * 1978-10-09 1980-04-15 Hitachi Ltd Method and apparatus for washing strainer
JPH06313504A (en) * 1993-04-30 1994-11-08 Toshiba Eng Co Ltd Strainer cleaner
JP2005066450A (en) * 2003-08-22 2005-03-17 Japan Organo Co Ltd Filtration apparatus
JP2012020260A (en) * 2010-07-16 2012-02-02 Mitsubishi Heavy Ind Ltd Apparatus for removing foreign matter in seawater

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5551412A (en) * 1978-10-09 1980-04-15 Hitachi Ltd Method and apparatus for washing strainer
JPH06313504A (en) * 1993-04-30 1994-11-08 Toshiba Eng Co Ltd Strainer cleaner
JP2005066450A (en) * 2003-08-22 2005-03-17 Japan Organo Co Ltd Filtration apparatus
JP2012020260A (en) * 2010-07-16 2012-02-02 Mitsubishi Heavy Ind Ltd Apparatus for removing foreign matter in seawater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627191A (en) * 2019-09-06 2019-12-31 中信环境技术(广州)有限公司 Pretreatment solid-liquid separation device and method
CN111167771A (en) * 2020-02-17 2020-05-19 青岛诺诚化学品安全科技有限公司 Online closed cleaning and detecting system and technological method for flame arrester

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