WO2013179371A1 - Soot removal device within flow path and dust collection device - Google Patents

Soot removal device within flow path and dust collection device Download PDF

Info

Publication number
WO2013179371A1
WO2013179371A1 PCT/JP2012/063626 JP2012063626W WO2013179371A1 WO 2013179371 A1 WO2013179371 A1 WO 2013179371A1 JP 2012063626 W JP2012063626 W JP 2012063626W WO 2013179371 A1 WO2013179371 A1 WO 2013179371A1
Authority
WO
WIPO (PCT)
Prior art keywords
dust
suction pipe
flow path
suction
flow passage
Prior art date
Application number
PCT/JP2012/063626
Other languages
French (fr)
Japanese (ja)
Inventor
暁 村井
康史 奥田
田中 敏彦
Original Assignee
三菱重工プラント建設株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 三菱重工プラント建設株式会社 filed Critical 三菱重工プラント建設株式会社
Priority to JP2012542285A priority Critical patent/JP5272111B1/en
Priority to IN2148MUN2014 priority patent/IN2014MN02148A/en
Priority to PCT/JP2012/063626 priority patent/WO2013179371A1/en
Publication of WO2013179371A1 publication Critical patent/WO2013179371A1/en

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J3/00Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
    • F23J3/02Cleaning furnace tubes; Cleaning flues or chimneys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G1/00Non-rotary, e.g. reciprocated, appliances
    • F28G1/16Non-rotary, e.g. reciprocated, appliances using jets of fluid for removing debris
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G15/00Details
    • F28G15/04Feeding and driving arrangements, e.g. power operation

Definitions

  • the present invention relates to an in-flow passage dedusting device and a dust collecting device.
  • a flue gas denitration method using a selective catalytic reduction reaction using ammonia (NH 3 ) as a reducing agent is used. Yes.
  • NH 3 is injected into NOx contained in the exhaust gas and reduced by a denitration catalyst.
  • denitration is performed by arranging a lattice-shaped denitration catalyst in a flow path through which exhaust gas flows such as an exhaust duct or a flow path casing connected to the exhaust duct.
  • the exhaust gas from a thermal power plant that uses coal as fuel contains a large amount of dust and other dust as unburned components, which causes clogging of the denitration catalyst.
  • a technique is known in which soot is blown off along the flow direction of exhaust gas by using a removal apparatus (suit blower) as described in Patent Document 1, for example.
  • popcorn ash By the way, depending on the nature of the coal, the operating conditions of the boiler, etc., a lump of soot is formed in the exhaust gas (particle diameter is several mm to several tens of mm) larger than the gas narrow flow path of the denitration catalyst (hereinafter referred to as popcorn ash)
  • the problem is that popcorn ash is clogged with the denitration catalyst and clogs the fine channels formed in a lattice shape in the denitration catalyst.
  • popcorn ash is larger than the gas flow path of the denitration catalyst, so it cannot be blown off along the flow direction of exhaust gas with a conventional denitrification device. It was necessary to clean it manually.
  • the present invention has been made in consideration of such circumstances, and its object is to provide a flow path capable of removing dust that is difficult to remove by spraying, such as popcorn ash, while the fluid is circulated in the flow path.
  • An object of the present invention is to provide an internal dust removal device and a dust collection device.
  • An in-flow channel decontamination device of the present invention is provided in a flow path casing through which a fluid flows, and dust that is contained in the fluid and accumulates in the flow path casing is allowed to flow through the flow path casing.
  • An in-flow channel degreasing device for removing, in order to suck the dust on the base end side while opening the front end facing the removal portion from which dust is removed, extending outward from the flow channel casing A suction pipe connected to the suction means, and a drive means for advancing and retracting the opening of the suction pipe in the flow path.
  • the suction pipe includes a distal end pipe having the opening facing the removal portion, a proximal end connected to the suction unit, and a distal end inserted into the distal end pipe. It is preferable that the driving means advance and retract the tip tube.
  • the suction pipe is divided into a distal end tube that advances and retracts and a fixed proximal end tube, and the proximal end tube is inserted into the distal end tube to reduce the occupied area of the suction tube.
  • the driving means may be configured to advance and retract the distal end tube through a moving interlocking shaft provided along the distal end tube and the proximal end tube.
  • the system in which the gas containing the dust sucked by the tip tube flows is arranged away from the system including the driving means, and therefore it is possible to prevent the driving means from being damaged by the heat of the gas. .
  • the removal portion in the flow-path casing is provided with a net for capturing dust, and the opening of the suction pipe is provided to face the net. According to the above configuration, it is possible to prevent dust larger than the mesh of the mesh from reaching the downstream side of the mesh.
  • the dust is more easily sucked by crushing the dust, and larger dust can be sucked by crushing the dust larger than the opening of the suction pipe.
  • the in-flow path defoaming device it is preferable to include a blowing means for blowing a dust removing gas to the removal portion.
  • a blowing means for blowing a dust removing gas to the removal portion.
  • the removing unit is a lattice-shaped denitration catalyst in which a plurality of narrow channels extend along the flow channel casing, and the suction pipe is provided on the upstream side of the denitration catalyst. Preferably it is.
  • a motor constituting the driving unit is provided apart from the suction pipe. According to the said structure, damage to the motor by the heat
  • the present invention provides any one of the above-described in-flow passage removal devices, a dust delivery pipe connected to the proximal end side of the suction pipe, a filter for capturing dust in the dust delivery pipe, and the suction means.
  • a dust collecting device is provided.
  • the dust collection device preferably includes means for introducing a cooling gas on the dust delivery pipe and upstream of the filter. According to the above configuration, it is possible to prevent high temperature fluid from reaching the filter by introducing cooling air to lower the temperature of the fluid.
  • the dust collection apparatus 1 of this embodiment is provided in the flow-path casing 4 connected with the exhaust duct 2a of the coal-fired boiler 2 of a thermal power plant, for example.
  • the dust collecting apparatus 1 removes dust such as soot adhering to the denitration catalyst 3 (removal part) mounted inside the flow path casing 4, in particular, a lump of soot having a large particle diameter called popcorn ash. It is for removing while circulating the fluid.
  • At least one denitration catalyst 3 is mounted inside the flow passage casing 4 through which the exhaust gas as a fluid flows, and nitrogen oxide (NOx) contained in the exhaust gas comes into contact with the exhaust gas flowing through the flow passage casing 4. It is to reduce.
  • the denitration catalyst 3 is arranged at a predetermined interval so that the exhaust gas sequentially passes.
  • the cross-sectional shape orthogonal to the exhaust gas flow direction F of the denitration catalyst 3 is a rectangular shape, and the flow path casing 4 has a shape in accordance with the shape of the denitration catalyst 3.
  • the denitration catalyst 3 has a predetermined thickness in the flow direction.
  • a plurality of narrow channels 3a along the flow direction F are formed in a grid pattern.
  • the denitration catalyst 3 has a lattice shape as viewed from the flow direction F.
  • One end side and the other end side in the flow direction of the denitration catalyst 3 form a flat surface (hereinafter referred to as an end face 3b), and the plurality of narrow channels 3a extend so as to connect the end faces.
  • the denitration catalyst 3 is mounted such that the end surface 3 b of the denitration catalyst 3 is orthogonal to the outer wall 4 a of the flow path casing 4.
  • the dust collecting device 1 is fixed to the outer wall 4 a of the flow channel casing 4, and has at least one in-channel removal device 6 provided for one denitration catalyst 3. And a dust processing unit 5 for discharging the dust removed by the removal device 6.
  • the dust processing unit 5 includes a dust delivery pipe 7 for delivering a gas containing dust removed by the in-flow passage removing device 6 (hereinafter referred to as a gas), a bug filter 8 for supplementing the dust contained in the gas, It has a fan 9 as a suction means for generating a suction force in the in-flow path removal device 6 through the dust delivery pipe 7. At least one dust processing unit 5 is provided in the dust collecting device 1 and configured to be able to process the dust sucked by the plurality of in-flow path removing devices 6.
  • the in-flow passage removing device 6 is a device that uses the negative pressure generated by the fan 9 to suck dust on the end surface 3 b of the denitration catalyst 3 mounted inside the flow passage casing 4. Details of the structure of the in-channel removal apparatus 6 will be described later.
  • One dust processing unit 5 is provided for the plurality of in-flow path de-greasing devices 6, and it is possible to select which in-flow path de-dusting device 6 the suction force of the fan 9 is applied to.
  • the dust delivery pipe 7 is a pipe that connects the in-flow path deguiding device 6 and the fan 9.
  • the dust distribution pipe 7 will be described with the in-flow passage removal device 6 side as the upstream side and the fan 9 side as the downstream side.
  • the gas flowing into the fan 9 from the upstream side is sent to the flue via the fan 9.
  • a bug filter 8 for supplementing the dust flowing through the dust delivery tube 7 is provided on the dust delivery tube 7.
  • the bag filter 8 for example, a non-woven fabric can be used as a filter medium, and dust contained in the gas flowing through the dust delivery pipe 7 can be deposited on the non-woven fabric surface. The dust captured by the bag filter 8 is sent to the ash treatment facility.
  • a temperature transmitter 11 is provided on the upstream side of the bag filter 8, and the temperature of the gas introduced into the bag filter 8 is measured.
  • the temperature transmitter 11 is connected to the temperature control device 12.
  • An air introduction valve 13 capable of introducing air as a cooling gas is provided on the upstream side of the temperature transmitter 11.
  • the air introduction valve 13 is connected to the temperature control device 12.
  • the temperature control device 12 cools the dust delivery pipe 7 by opening the atmosphere introduction valve 13.
  • the temperature of the gas can be lowered by introducing air as a gas.
  • a pressure transmitter 14 for measuring the pressure in the dust delivery pipe 7 is provided on the upstream side of the air introduction valve 13.
  • the pressure transmitter 14 is connected to the pressure control device 15.
  • a suction force control valve 16 is provided downstream of the bag filter 8 and upstream of the fan 9.
  • the suction force control valve 16 is connected to the pressure control device 15.
  • the pressure control device 15 is set to adjust the suction force control valve 16 so that the gas pressure measured by the pressure transmitter 14 becomes a predetermined pressure.
  • the dust delivery pipe 7 on the upstream side of the pressure transmitter 14 is branched into a plurality of branch passages 7a, and each is connected to the in-flow passage removing device 6.
  • a switching valve 17 is provided in each branch path 7a.
  • the switching valve 17 is a valve that is opened and closed by a control device (not shown).
  • the switching valve 17 generates a suction force of the fan 9 in the in-flow passage removing device 6 in the open state, and blocks the suction force of the fan 9 in the closed state.
  • the in-flow channel removing device 6 has a lance tube 21 that is a tip tube inserted into the flow channel casing 4, and the tip is opened facing the denitration catalyst 3.
  • a suction pipe 20 extending outward from the flow path casing 4, a housing 22 disposed outside the flow path casing 4 and accommodating a part of the suction pipe 20, and a drive mechanism 23 (drive means) for moving the lance tube 21 forward and backward )
  • the housing 22 has a rectangular tube shape.
  • a terminal box 29 that accommodates a control board and the like is provided on the side surface of the housing 22.
  • the in-flow channel removing device 6 is attached to the outer wall 4 a of the flow channel casing 4 through a wall box 24. Further, the in-flow channel removing device 6 is attached so that the longitudinal direction of the lance tube 21 (hereinafter simply referred to as the longitudinal direction) is along the end surface 3 b of the denitration catalyst 3.
  • the suction pipe 20 has a lance tube 21 and a feed pipe 25 (base pipe) fitted into the lance tube 21.
  • the feed pipe 25 is connected to the fan 9 (see FIG. 1) via the dust delivery pipe 7 on the base end side, that is, the side opposite to the lance tube 21 in the longitudinal direction.
  • the feed pipe 25 is a circular tube-shaped member whose base end side is supported in a cantilever manner on the housing 22, and a distal end side is inserted into the circular tube-shaped lance tube 21.
  • the lance tube 21 is a circular tube-shaped member that is fitted to the distal end side of the feed pipe 25 and that can be moved forward and backward in the longitudinal direction by the drive mechanism 23.
  • the lance tube 21 is composed of a lance tube main body 26 combined with the feed pipe 25 along the longitudinal direction, and a suction pipe portion 27 provided on the distal end side of the lance tube main body 26. Further, the lance tube 21 is inserted into the flow passage casing 4 through the wall box 24 while the distal end side including the suction pipe portion 27 protrudes to the outside of the housing 22.
  • the lance tube main body 26 is bent in the direction along the flow direction F of the flow path casing 4 and toward the denitration catalyst 3, and the suction pipe portion 27 is connected to the bent end portion. ing.
  • the suction pipe portion 27 has a circular tube shape like the lance tube main body 26, and its longitudinal direction is orthogonal to the longitudinal direction of the lance tube main body 26 and orthogonal to the flow direction F of the flow path casing 4. Is formed. That is, the suction pipe portion 27 is formed along the end surface 3 b of the denitration catalyst 3.
  • suction pipe part 27 The both ends of the suction pipe part 27 are closed.
  • a plurality of suction ports 28 are formed along the longitudinal direction of the suction pipe portion 27 on the side of the suction pipe portion 27 facing the denitration catalyst 3.
  • the shape of the suction port 28 is an oval shape along the longitudinal direction of the suction pipe portion 27.
  • the drive mechanism 23 includes a traveling carriage 30 attached to the proximal end of the lance tube 21, a motor 33 provided outside the housing 22, and a sprocket and chain that transmits the power of the motor 33 to the traveling carriage 30. Have.
  • a traveling carriage 30 that holds the lance tube 21 in a reciprocating manner along the longitudinal direction of the housing 22 is provided at the base end of the lance tube 21.
  • the traveling carriage 30 holds the proximal end of the lance tube 21 and has a shape covering the outer periphery of the feed pipe 25, and has a function of keeping the airtightness between the lance tube 21 and the feed pipe 25. .
  • a sealing member 31 that seals between the inner peripheral surface of the traveling carriage 30 and the outer peripheral surface of the feed pipe 25 is provided on the contact surface of the traveling carriage 30 with the feed pipe 25.
  • a gland packing can be employed as the sealing member 31, for example.
  • a guide roller 40 that travels on a guide rail 32 provided along the longitudinal direction of the housing 22 is attached to the traveling carriage 30, whereby a lance tube held by the traveling carriage 30 is installed. The movement along the longitudinal direction of 21 is enabled. Further, the guide roller 40 is provided at a position where it can abut on limit switches 45 and 46, which will be described later, and turn the limit switch ON / OFF.
  • a motor 33 is disposed outside the housing 22 on the base end side of the housing 22.
  • a first sprocket 34 is attached to the output shaft of the motor 33, and a second sprocket 35 is attached to the proximal end side inside the housing 22.
  • a first chain 36 is hung on the first sprocket 34 and the second sprocket 35 so as to form an elliptical track. That is, the power of the motor 33 is transmitted via the first sprocket 34, the first chain 36, and the second sprocket 35 to the first rotating shaft 37 that rotatably supports the second sprocket 35.
  • a third sprocket 38 that rotates together with the second sprocket 35 is attached to a first rotating shaft 37 that is rotatably attached to the proximal end side of the housing 22.
  • a second rotary shaft 39 is attached to the front end side of the housing 22 so as to avoid interference with the suction pipe 20, and a fourth sprocket 41 is rotatably attached to the second rotary shaft 39.
  • a second chain 42 is hung on the third sprocket 38 and the fourth sprocket 41, whereby the second chain 42 forms an elliptical track along the longitudinal direction of the housing 22. Further, the second chain 42 is coupled to the traveling carriage 30 via the connection member 43.
  • the third sprocket 38 rotates and the second chain 42 rotates on its track. Since the second chain 42 is connected to the traveling carriage 30, the traveling carriage 30 moves along the longitudinal direction when the second chain 42 travels on the track. That is, the lance tube 21 integrated with the traveling carriage 30 is moved along the longitudinal direction by the power of the motor 33.
  • a reverse limit switch 45 is provided on the distal end side of the housing 22, and a stop limit switch 46 is provided on the proximal end side of the housing 22.
  • the limit switches 45 and 46 are arranged so that the switch is turned on when the guide roller 40 of the traveling carriage 30 comes into contact.
  • the limit switches 45 and 46 control the movement range of the lance tube 21 and the traveling carriage 30 and control the forward and reverse movements.
  • the wall box 24 includes a rectangular parallelepiped box body 47 and a seal box 48 attached to the base end side of the box body 47.
  • the box body 47 is formed with a through hole 49 through which the lance tube 21 passes through a surface facing the distal end side and a surface facing the base end side opposite thereto. A predetermined gap is provided between the through hole 49 and the lance tube 21.
  • the seal box 48 is a rectangular parallelepiped box-like member, and is provided on the base end side of the box body 47.
  • the seal box 48 is connected to a high pressure seal air supply pipe 50 for maintaining the inside of the seal box 48 at a high pressure.
  • the air supplied from the high-pressure seal air supply pipe 50 flows into the box body 47 through a gap between the through hole 49 on the base end side of the box body 47 and the outer peripheral surface of the lance tube 21.
  • An attachment stay 51 extends on the proximal end side of the box body 47 and is connected to an attachment stay 52 provided on the distal end side of the housing 22.
  • a support roller 53 that supports the lance tube 21 from below is provided on the front end side of the housing 22.
  • the operation of the dust collection device 1 will be described.
  • the second chain 42 travels by the rotational force of the motor 33, and the lance tube 21 extends along the longitudinal direction via the connecting member 43 and the traveling carriage 30 connected to the second chain 42.
  • the lance tube 21 is controlled by a control device (not shown) so as to move forward in the direction of the distal end until the reverse limit switch 45 is turned on and to move backward until the stop limit switch 46 is turned on.
  • the dust on the denitration catalyst 3 is sucked and the gas containing the dust flows into the dust delivery pipe 7 through the feed pipe 25.
  • the pressure of the gas is measured by the pressure transmitter 14, and the suction force control valve 16 is controlled according to this pressure, and the suction force is controlled.
  • the temperature of the gas is measured by the temperature transmitter 11, and the air introduction valve 13 is controlled according to this temperature, and the temperature of the gas is controlled.
  • dust contained in the gas is captured by the bag filter 8 and sent to the ash treatment facility.
  • the gas from which the dust has been removed is sent to the flue via the fan 9.
  • the dust adhering to the denitration catalyst 3, in particular, the lump of the soot having a large particle diameter such as popcorn ash is sucked and removed through the suction pipe 20 of the in-channel degutting device 6. Therefore, dust can be prevented from accumulating on the denitration catalyst 3. Thereby, the continuous operation time of a plant can be made longer. Moreover, since the dust in the flow path casing 4 is discharged
  • the inside of the seal box 48 is maintained at a higher pressure than the inside of the flow path casing 4, it is possible to prevent the exhaust gas from leaking out from the insertion portion of the suction pipe 20.
  • the box body 47 is provided between the seal box 48 and the flow path casing 4, but the box body 47 of the wall box 24 may be omitted.
  • the in-flow channel removal apparatus 6 ⁇ / b> B according to the second embodiment has a suction pipe 20 and a wall box compared to the in-flow path removal apparatus 6 (see FIG. 3) of the first embodiment.
  • the structure of 24B is different.
  • the suction pipe 20B of the present embodiment is provided in parallel with the moving interlocking shaft 55 that can be moved back and forth in the longitudinal direction by the drive mechanism 23, and the moving interlocking shaft 55, and the base end side is cantilevered to the wall box 24B.
  • a lance tube 21 ⁇ / b> B that is provided in parallel to the moving interlocking shaft 55 and connected to the moving interlocking shaft 55.
  • the front end side of the feed pipe 25B is inserted into the lance tube 21B.
  • the moving interlocking shaft 55 passes through the wall box 24B and extends to the inside of the flow path casing 4, and the tip thereof is connected to the lance tube 21B. That is, the lance tube 21B is configured to advance and retract in the longitudinal direction when the moving interlocking shaft 55 advances and retracts.
  • the lance tube 21B can advance and retreat in a telescopic manner on the feed pipe 25B while sealing between the inner peripheral surface of the lance tube 21B and the outer peripheral surface of the feed pipe 25B.
  • a sealing mechanism 56 is provided.
  • a labyrinth seal 57 is provided on the contact surface of the seal mechanism 56 with the feed pipe 25B.
  • the lance tube 21B includes a lance tube main body 26B, a first suction pipe portion 58 provided at the tip of the lance tube main body 26B, and a second suction pipe portion 59 provided at the base end of the lance tube main body.
  • the lance tube 21B of the present embodiment has two suction pipe portions 58, 59.
  • the first suction pipe portion 58 is on one side in the longitudinal direction of the denitration catalyst 3, and the second suction pipe portion 59 is denitration. The other side in the longitudinal direction of the catalyst 3 is sucked.
  • the movement interlocking shaft 55 advances and retreats in the longitudinal direction by driving the motor 33.
  • the lance tube 21B connected to the moving interlocking shaft 55 advances and retreats in the longitudinal direction.
  • the gas containing the dust sucked by the lance tube 21B is sent to the dust delivery pipe 7 without passing through the inside of the housing 22, so that the inside of the housing 22 is prevented from being damaged by the heat of the gas. can do.
  • the suction pipe portions 58 and 59 are attached to the distal end and the proximal end of the lance tube 21B, the stroke of the lance tube 21B is substantially halved as compared with the in-flow passage deguiding device 6 of the first embodiment. can do.
  • FIG. 7 is a partially enlarged view for explaining another form of the in-flow channel degreasing device.
  • another embodiment of the in-flow passage removing apparatus 6 ⁇ / b> C is provided with a wire net 61 that is a net for capturing dust on the upstream side of the denitration catalyst 3.
  • the mesh of the wire mesh 61 is set to a size that can complement the large lump of candy such as popcorn ash and prevent passage of the cocoon lump.
  • the wire net 61 is disposed immediately before the denitration catalyst 3.
  • the suction port 28 of the lance tube 21 is provided to face the wire mesh 61.
  • the lance tube 21 of the in-flow passage removing apparatus 6C of the present embodiment is provided with a brush 62 as a crushing means for crushing dust.
  • the brush 62 includes a support portion 63 that protrudes from the lance tube main body 26 toward the distal end side, and a number of metal wires 64 welded to the support portion 63, and the distal end of the wire 64 is the wire mesh 61. Projecting toward the metal mesh 61 and the denitration catalyst 3 side.
  • FIG. 8 is a partially enlarged view for explaining still another embodiment of the in-flow passage removing apparatus, and is a plan view of the lance tube 21D and the suction pipe portion 27D as viewed from the direction along the flow direction F.
  • the lance tube main body 26 of each of the above embodiments is connected to the suction pipe portion 27D of the in-flow passage removing apparatus 6D of the present embodiment, and high-pressure air that is a dust removing gas is used.
  • the injection pipe 65 has substantially the same configuration as the suction pipe 20, but the suction pipe 20 sucks dust from the suction pipe portion 27D by the suction force of the fan 9, whereas the injection pipe 65 has a high-pressure air. Is different in that air is ejected from the suction port 28 of the suction pipe portion 27D.
  • the form for supplying high-pressure air is not limited to this, and as shown in FIG. 9, a separate injection pipe portion 67 is provided, and an injection pipe 65 for supplying high-pressure air is connected to this injection pipe portion 67. It is good also as a structure. Moreover, as shown in FIG. 9, the injection pipe part 67 is good also as a structure which provides two so that the suction pipe part 27D may be pinched
  • the method for removing the dust contained in the gas is not limited to the bag filter, and the dust in the gas may be separated using a powder separator (cyclone). Or it is good also as a structure which throws in gas again in the location which does not have trouble in the process in a plant, without removing the dust in gas on the dust delivery pipe
  • the dust collection device according to each of the above embodiments can collect not only popcorn ash but also various sizes of dust as long as it can be sucked by the suction pipe.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Chimneys And Flues (AREA)
  • Incineration Of Waste (AREA)
  • Cyclones (AREA)

Abstract

Provided is a soot removal device, disposed in a flow path through which a fluid flows, for the purpose of removing dust contained in the fluid and deposited in the flow path, while circulating the fluid through the flow path, said soot removal device being provided with: a suction pipe (20) that extends outward from a flow path casing (4) and has an open leading end (21) facing a removal part (3) from which dust is to be removed, said suction pipe (20) being connected to a suction means (9) at the base end side; and a drive means (23) for causing forward and backward movement of the opening of the suction pipe (20) in the flow path.

Description

流路内除煤装置及び塵埃回収装置Passage removal device and dust collection device
 本発明は、流路内除煤装置及び塵埃回収装置に関する。 The present invention relates to an in-flow passage dedusting device and a dust collecting device.
 例えば火力発電プラントから排出される塵埃を含む排ガス中の窒素酸化物(NOx)を除去するために、アンモニア(NH)を還元剤とする選択的接触還元反応による排煙脱硝法が用いられている。この選択的接触還元反応は、排ガス中に含まれるNOxに対してNHを注入して脱硝触媒により還元するものである。具体的には、排気ダクトや、排気ダクトに連結された流路ケーシングなどの排ガスが流れる流路に格子状の脱硝触媒を配置することによって脱硝を行っている。 For example, in order to remove nitrogen oxides (NOx) in exhaust gas containing dust discharged from a thermal power plant, a flue gas denitration method using a selective catalytic reduction reaction using ammonia (NH 3 ) as a reducing agent is used. Yes. In this selective catalytic reduction reaction, NH 3 is injected into NOx contained in the exhaust gas and reduced by a denitration catalyst. Specifically, denitration is performed by arranging a lattice-shaped denitration catalyst in a flow path through which exhaust gas flows such as an exhaust duct or a flow path casing connected to the exhaust duct.
 石炭を燃料とする火力発電プラントの排ガスは、未燃分として煤などの塵埃を多量に含むため、これにより脱硝触媒の目詰まりが発生する。この問題を解決するため、例えば特許文献1に記載されているような除煤装置(スーツブロワ)によって、煤を排ガスの流れ方向に沿って吹き飛ばす技術が知られている。 The exhaust gas from a thermal power plant that uses coal as fuel contains a large amount of dust and other dust as unburned components, which causes clogging of the denitration catalyst. In order to solve this problem, for example, a technique is known in which soot is blown off along the flow direction of exhaust gas by using a removal apparatus (suit blower) as described in Patent Document 1, for example.
特開昭62-69015号公報JP-A-62-69015
 ところで、石炭の性質やボイラの運転条件などにより、排ガス中に脱硝触媒のガス細流路より大きな(粒径が数mmから十数mm)煤の塊が形成され(以下ポップコーンアッシュと言う)、このポップコーンアッシュが脱硝触媒に詰まって、脱硝触媒に格子状に形成されている細流路を閉塞させてしまうことが問題となっている。粒子状の煤とは異なり、ポップコーンアッシュは脱硝触媒のガス流路より大きい為、従来の除煤装置で排ガスの流れ方向に沿って吹き飛ばせず、その除去のためには、プラントと停止させて人力で清掃する必要があった。 By the way, depending on the nature of the coal, the operating conditions of the boiler, etc., a lump of soot is formed in the exhaust gas (particle diameter is several mm to several tens of mm) larger than the gas narrow flow path of the denitration catalyst (hereinafter referred to as popcorn ash) The problem is that popcorn ash is clogged with the denitration catalyst and clogs the fine channels formed in a lattice shape in the denitration catalyst. Unlike particulate soot, popcorn ash is larger than the gas flow path of the denitration catalyst, so it cannot be blown off along the flow direction of exhaust gas with a conventional denitrification device. It was necessary to clean it manually.
 この発明は、このような事情を考慮してなされたもので、その目的は、流路内に流体を流通したままでも、ポップコーンアッシュのような吹き付けによる除去が困難な塵埃でも除去可能な流路内除煤装置及び塵埃回収装置を提供することにある。 The present invention has been made in consideration of such circumstances, and its object is to provide a flow path capable of removing dust that is difficult to remove by spraying, such as popcorn ash, while the fluid is circulated in the flow path. An object of the present invention is to provide an internal dust removal device and a dust collection device.
 上記課題を解決するために、この発明は以下の手段を提供している。
 本発明の流路内除煤装置は、流体が流れる流路ケーシングに設けられ、前記流体に含まれて前記流路ケーシング内に堆積する塵埃を、前記流路ケーシング内に前記流体を流通させつつ除去するための流路内除煤装置であって、塵埃が除去される除去部に対向して先端が開口し、前記流路ケーシングから外側へと延びるとともに、基端側で塵埃を吸引するための吸引手段と接続される吸込管と、前記吸込管の開口を流路内で進退させる駆動手段とを備えることを特徴とする。
In order to solve the above problems, the present invention provides the following means.
An in-flow channel decontamination device of the present invention is provided in a flow path casing through which a fluid flows, and dust that is contained in the fluid and accumulates in the flow path casing is allowed to flow through the flow path casing. An in-flow channel degreasing device for removing, in order to suck the dust on the base end side while opening the front end facing the removal portion from which dust is removed, extending outward from the flow channel casing A suction pipe connected to the suction means, and a drive means for advancing and retracting the opening of the suction pipe in the flow path.
 上記構成によれば、塵埃を吸込管を介して吸引して除去する構成としたため、塵埃が除去部に堆積することを防止することができる。 According to the above configuration, since dust is sucked and removed through the suction pipe, it is possible to prevent dust from accumulating on the removal portion.
 上記流路内除煤装置において、前記吸込管は、前記除去部に対向する前記開口を有する先端管と、基端が前記吸引手段と接続され、先端が前記先端管の内部に挿入された基端管とを有し、前記駆動手段は、前記先端管を進退させることが好ましい。 In the above-described flow passage removing apparatus, the suction pipe includes a distal end pipe having the opening facing the removal portion, a proximal end connected to the suction unit, and a distal end inserted into the distal end pipe. It is preferable that the driving means advance and retract the tip tube.
 上記構成によれば、吸込管を進退する先端管と固定される基端管とに分割し、基端管が先端管内部に挿入されるように組み合わせることによって、吸込管の占有面積を小さくし、流路内除煤装置を小型化することができる。 According to the above configuration, the suction pipe is divided into a distal end tube that advances and retracts and a fixed proximal end tube, and the proximal end tube is inserted into the distal end tube to reduce the occupied area of the suction tube. In addition, it is possible to reduce the size of the in-channel removal apparatus.
 上記流路内除煤装置において、前記駆動手段は、前記先端管及び前記基端管に沿って設けられた移動用連動軸を介して前記先端管を進退させる構成としてもよい。 In the in-channel removal apparatus, the driving means may be configured to advance and retract the distal end tube through a moving interlocking shaft provided along the distal end tube and the proximal end tube.
 上記構成によれば、先端管によって吸引された塵埃を含むガスが流れる系統を、駆動手段を含む系統とが離間して配置されるため、ガスの熱による駆動手段の損傷を防止することができる。 According to the above configuration, the system in which the gas containing the dust sucked by the tip tube flows is arranged away from the system including the driving means, and therefore it is possible to prevent the driving means from being damaged by the heat of the gas. .
 上記流路内除煤装置において、前記流路ケーシング内の前記除去部には、塵埃を捕捉する網が設けられ、前記吸込管の前記開口は前記網に対向して設けられることが好ましい。
 上記構成によれば、網の目より大きい塵埃が網よりも後流側に及ぶことを防止することができる。
In the above-described in-channel removal apparatus, it is preferable that the removal portion in the flow-path casing is provided with a net for capturing dust, and the opening of the suction pipe is provided to face the net.
According to the above configuration, it is possible to prevent dust larger than the mesh of the mesh from reaching the downstream side of the mesh.
 上記流路内除煤装置において、前記網に捕捉された塵埃を破砕する破砕手段を備えることが好ましい。
 上記構成によれば、塵埃を砕くことによって、塵埃がより吸引されやすくなるとともに、吸込管の開口よりも大きい塵埃を破砕することによって、より大きな塵埃を吸引することができる。
In the above-mentioned flow path removal apparatus, it is preferable to include crushing means for crushing dust captured by the net.
According to the above configuration, the dust is more easily sucked by crushing the dust, and larger dust can be sucked by crushing the dust larger than the opening of the suction pipe.
 上記流路内除煤装置において、前記除去部に塵埃除去用気体を吹き付ける吹き付け手段を備えることが好ましい。
 上記構成によれば、塵埃除去用気体を塵埃に吹き付けて塵埃を浮遊させることによって、塵埃の吸引効率を向上させることができる。
In the in-flow path defoaming device, it is preferable to include a blowing means for blowing a dust removing gas to the removal portion.
According to the above configuration, the dust suction efficiency can be improved by blowing the dust removing gas to the dust to float the dust.
 上記流路内除煤装置において、前記除去部は複数の細流路が前記流路ケーシングに沿って延在する格子状の脱硝触媒であり、前記吸込管は前記脱硝触媒の上流側に設けられていることが好ましい。 In the in-flow channel removing apparatus, the removing unit is a lattice-shaped denitration catalyst in which a plurality of narrow channels extend along the flow channel casing, and the suction pipe is provided on the upstream side of the denitration catalyst. Preferably it is.
 上記流路内除煤装置において、前記駆動手段を構成するモータが前記吸込管に対して離間して設けられていることが好ましい。
 上記構成によれば、塵埃を含むガスの熱によるモータの損傷を防止することができる。
In the above-described in-channel removal apparatus, it is preferable that a motor constituting the driving unit is provided apart from the suction pipe.
According to the said structure, damage to the motor by the heat | fever of the gas containing dust can be prevented.
 また、本発明は、上記いずれかの流路内除煤装置と、前記吸込管の基端側に接続された塵埃配送管と、前記塵埃配送管の塵埃を捕捉するフィルタと、前記吸引手段とを備えることを特徴とする塵埃回収装置を提供する。 In addition, the present invention provides any one of the above-described in-flow passage removal devices, a dust delivery pipe connected to the proximal end side of the suction pipe, a filter for capturing dust in the dust delivery pipe, and the suction means. A dust collecting device is provided.
 上記構成によれば、塵埃を排出するための塵埃配送管にフィルタを設けることにより、流路内除煤装置によって吸引された塵埃を補足することができる。 According to the above configuration, by providing the filter in the dust delivery tube for discharging the dust, it is possible to supplement the dust sucked by the in-flow passage removing device.
 上記塵埃回収装置において、前記塵埃配送管上であって、前記フィルタの上流側に冷却気体を導入する手段を備えることが好ましい。
 上記構成によれば、冷却空気を導入して流体の温度を下げることによって、高温の流体がフィルタに及ぶことを防止することができる。
The dust collection device preferably includes means for introducing a cooling gas on the dust delivery pipe and upstream of the filter.
According to the above configuration, it is possible to prevent high temperature fluid from reaching the filter by introducing cooling air to lower the temperature of the fluid.
 本発明によれば、塵埃を吸込管を介して吸引して除去する構成としたため、塵埃が除去部に堆積することを防止することができる。 According to the present invention, since dust is sucked and removed through the suction pipe, dust can be prevented from accumulating on the removal portion.
本発明の実施形態に係る塵埃回収装置の系統図である。It is a systematic diagram of the dust collection | recovery apparatus which concerns on embodiment of this invention. 塵埃回収装置の脱硝触媒を示す斜視図である。It is a perspective view which shows the denitration catalyst of a dust collection | recovery apparatus. 本発明の第一実施形態に係る流路内除煤装置の側面図である。It is a side view of the in-channel removal apparatus according to the first embodiment of the present invention. 図3のA矢視図であり、本発明の第一実施形態に係る流路内除煤装置の平面図である。It is A arrow line view of FIG. 3, and is a top view of the in-flow path dehulling device which concerns on 1st embodiment of this invention. 図3のB部拡大図である。It is the B section enlarged view of FIG. 本発明の第二実施形態に係る流路内除煤装置の側面図である。It is a side view of the in-channel removal device concerning a second embodiment of the present invention. 流路内除煤装置の別の形態を説明する部分拡大図である。It is the elements on larger scale explaining another form of the removal apparatus in a flow path. 流路内除煤装置のさらに別の形態を説明する部分拡大図である。It is the elements on larger scale explaining further another form of the in-channel removal apparatus. 流路内除煤装置のさらに別の形態を説明する部分拡大図である。It is the elements on larger scale explaining further another form of the in-channel removal apparatus.
 以下、本発明の実施形態について図面を参照して詳細に説明する。
 図1に示すように、本実施形態の塵埃回収装置1は、例えば火力発電プラントの石炭焚きのボイラ2の排気ダクト2aに連結された流路ケーシング4に設けられている。塵埃回収装置1は、流路ケーシング4の内部に装着されている脱硝触媒3(除去部)に付着する煤などの塵埃、特にポップコーンアッシュと呼ばれる粒径の大きな煤の塊を、流路ケーシング4に流体を流通させつつ除去するためのものである。
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
As shown in FIG. 1, the dust collection apparatus 1 of this embodiment is provided in the flow-path casing 4 connected with the exhaust duct 2a of the coal-fired boiler 2 of a thermal power plant, for example. The dust collecting apparatus 1 removes dust such as soot adhering to the denitration catalyst 3 (removal part) mounted inside the flow path casing 4, in particular, a lump of soot having a large particle diameter called popcorn ash. It is for removing while circulating the fluid.
 脱硝触媒3は、流体である排ガスが流れる流路ケーシング4の内部に少なくとも1つ装着されており、この流路ケーシング4を流れる排ガスと接触して排ガス中に含まれる窒素酸化物(NOx)を低減するものである。例えば脱硝触媒3は排ガスが順次通過するように所定の間隔をおいて配置されている。 At least one denitration catalyst 3 is mounted inside the flow passage casing 4 through which the exhaust gas as a fluid flows, and nitrogen oxide (NOx) contained in the exhaust gas comes into contact with the exhaust gas flowing through the flow passage casing 4. It is to reduce. For example, the denitration catalyst 3 is arranged at a predetermined interval so that the exhaust gas sequentially passes.
 図2に示すように、脱硝触媒3の排ガス流れ方向Fに直交する断面形状は、矩形形状であり、流路ケーシング4は脱硝触媒3の形状に則した形状となっている。脱硝触媒3は、流れ方向に所定の厚みを有している。脱硝触媒3には、流れ方向Fに沿う複数の細流路3aが碁盤の目状に形成されている。脱硝触媒3は、流れ方向Fから視て格子状をなしている。 As shown in FIG. 2, the cross-sectional shape orthogonal to the exhaust gas flow direction F of the denitration catalyst 3 is a rectangular shape, and the flow path casing 4 has a shape in accordance with the shape of the denitration catalyst 3. The denitration catalyst 3 has a predetermined thickness in the flow direction. In the denitration catalyst 3, a plurality of narrow channels 3a along the flow direction F are formed in a grid pattern. The denitration catalyst 3 has a lattice shape as viewed from the flow direction F.
 脱硝触媒3の流れ方向一端側及び他端側は平面(以下、端面3bと呼ぶ)をなし、複数の細流路3aはこの端面同士を接続するように延在している。脱硝触媒3は、脱硝触媒3の端面3bが流路ケーシング4の外壁4aと直交するように装着されている。 One end side and the other end side in the flow direction of the denitration catalyst 3 form a flat surface (hereinafter referred to as an end face 3b), and the plurality of narrow channels 3a extend so as to connect the end faces. The denitration catalyst 3 is mounted such that the end surface 3 b of the denitration catalyst 3 is orthogonal to the outer wall 4 a of the flow path casing 4.
 図1に示すように、塵埃回収装置1は、流路ケーシング4の外壁4aに固定され、一つの脱硝触媒3に対して少なくとも一つ設けられた流路内除煤装置6と、流路内除煤装置6によって除去された塵埃を排出する塵埃処理部5とを有している。 As shown in FIG. 1, the dust collecting device 1 is fixed to the outer wall 4 a of the flow channel casing 4, and has at least one in-channel removal device 6 provided for one denitration catalyst 3. And a dust processing unit 5 for discharging the dust removed by the removal device 6.
 塵埃処理部5は、流路内除煤装置6によって除去された塵埃を含むガス(以下、ガスと呼ぶ)を配送する塵埃配送管7と、ガスに含まれる塵埃を補足するバグフィルタ8と、塵埃配送管7を介して流路内除煤装置6に吸引力を生じさせる吸引手段としてのファン9とを有している。
 塵埃処理部5は、塵埃回収装置1に少なくとも一つ設けられており、複数の流路内除煤装置6によって吸引された塵埃を処理可能に構成されている。
The dust processing unit 5 includes a dust delivery pipe 7 for delivering a gas containing dust removed by the in-flow passage removing device 6 (hereinafter referred to as a gas), a bug filter 8 for supplementing the dust contained in the gas, It has a fan 9 as a suction means for generating a suction force in the in-flow path removal device 6 through the dust delivery pipe 7.
At least one dust processing unit 5 is provided in the dust collecting device 1 and configured to be able to process the dust sucked by the plurality of in-flow path removing devices 6.
 流路内除煤装置6は、ファン9によって生じる負圧を利用して、流路ケーシング4の内部に装着された脱硝触媒3の端面3b上の塵埃を吸引する装置である。流路内除煤装置6の構造の詳細については後述する。 The in-flow passage removing device 6 is a device that uses the negative pressure generated by the fan 9 to suck dust on the end surface 3 b of the denitration catalyst 3 mounted inside the flow passage casing 4. Details of the structure of the in-channel removal apparatus 6 will be described later.
 次に、塵埃処理部5について説明する。塵埃処理部5は、複数の流路内除煤装置6に対して一つ設けられており、ファン9による吸引力をどの流路内除煤装置6に働かせるかを選択することができる。 Next, the dust processing unit 5 will be described. One dust processing unit 5 is provided for the plurality of in-flow path de-greasing devices 6, and it is possible to select which in-flow path de-dusting device 6 the suction force of the fan 9 is applied to.
 塵埃配送管7は、流路内除煤装置6とファン9とを接続する配管である。以下の説明においては、塵埃配送管7の流路内除煤装置6側を上流側、ファン9側を下流側として説明する。上流側よりファン9に流入したガスは、ファン9を経由して煙道に送られる。 The dust delivery pipe 7 is a pipe that connects the in-flow path deguiding device 6 and the fan 9. In the following description, the dust distribution pipe 7 will be described with the in-flow passage removal device 6 side as the upstream side and the fan 9 side as the downstream side. The gas flowing into the fan 9 from the upstream side is sent to the flue via the fan 9.
 塵埃配送管7上には、塵埃配送管7を流れる塵埃を補足するためのバグフィルタ8が設けられている。バグフィルタ8としては、例えばろ材として不織布を用いて、塵埃配送管7を流れるガスに含まれる塵埃を不織布表面に堆積させるものを採用することができる。バグフィルタ8によって補足された塵埃は、灰処理設備へ送られる。 On the dust delivery tube 7, a bug filter 8 for supplementing the dust flowing through the dust delivery tube 7 is provided. As the bag filter 8, for example, a non-woven fabric can be used as a filter medium, and dust contained in the gas flowing through the dust delivery pipe 7 can be deposited on the non-woven fabric surface. The dust captured by the bag filter 8 is sent to the ash treatment facility.
 バグフィルタ8の上流側には温度発信器11が設けられており、バグフィルタ8に導入されるガスの温度が計測される。温度発信器11は、温度制御装置12と接続されている。温度発信器11の上流側には、冷却気体としての空気を導入することが可能な大気導入弁13が設けられている。大気導入弁13は、温度制御装置12と接続されている。
 温度制御装置12は、温度発信器11によって計測されるガスの温度が、所定の温度(例えば200℃)を超える場合に、大気導入弁13を開状態にすることにより、塵埃配送管7に冷却気体としての空気を導入してガスの温度を下げることができる。
A temperature transmitter 11 is provided on the upstream side of the bag filter 8, and the temperature of the gas introduced into the bag filter 8 is measured. The temperature transmitter 11 is connected to the temperature control device 12. An air introduction valve 13 capable of introducing air as a cooling gas is provided on the upstream side of the temperature transmitter 11. The air introduction valve 13 is connected to the temperature control device 12.
When the temperature of the gas measured by the temperature transmitter 11 exceeds a predetermined temperature (for example, 200 ° C.), the temperature control device 12 cools the dust delivery pipe 7 by opening the atmosphere introduction valve 13. The temperature of the gas can be lowered by introducing air as a gas.
 大気導入弁13の上流側には、塵埃配送管7内の圧力を測定する圧力発信器14が設けられている。圧力発信器14は、圧力制御装置15と接続されている。また、バグフィルタ8の下流側であって、ファン9の上流側には、吸引力制御弁16が設けられている。吸引力制御弁16は、圧力制御装置15と接続されている。
 圧力制御装置15は、圧力発信器14によって計測されるガスの圧力が、所定の圧力となるように、吸引力制御弁16を調整するように設定されている。
A pressure transmitter 14 for measuring the pressure in the dust delivery pipe 7 is provided on the upstream side of the air introduction valve 13. The pressure transmitter 14 is connected to the pressure control device 15. A suction force control valve 16 is provided downstream of the bag filter 8 and upstream of the fan 9. The suction force control valve 16 is connected to the pressure control device 15.
The pressure control device 15 is set to adjust the suction force control valve 16 so that the gas pressure measured by the pressure transmitter 14 becomes a predetermined pressure.
 圧力発信器14の上流側の塵埃配送管7は、複数の分岐路7aに分岐されており、それぞれ流路内除煤装置6に接続されている。それぞれの分岐路7aには、切替弁17が設けられている。切替弁17は、図示しない制御装置によって開閉される弁であり、開状態においてファン9の吸引力を流路内除煤装置6に生じさせるとともに、閉状態においてファン9の吸引力を遮断する。 The dust delivery pipe 7 on the upstream side of the pressure transmitter 14 is branched into a plurality of branch passages 7a, and each is connected to the in-flow passage removing device 6. A switching valve 17 is provided in each branch path 7a. The switching valve 17 is a valve that is opened and closed by a control device (not shown). The switching valve 17 generates a suction force of the fan 9 in the in-flow passage removing device 6 in the open state, and blocks the suction force of the fan 9 in the closed state.
 次に、流路内除煤装置6の詳細構造について説明する。
 図3及び図4に示すように、流路内除煤装置6は、流路ケーシング4に挿入される先端管であるランスチューブ21を有し、脱硝触媒3に対向して先端が開口し、流路ケーシング4から外側に延びている吸込管20と、流路ケーシング4の外部に配置され、吸込管20の一部を収容するハウジング22と、ランスチューブ21を進退させる駆動機構23(駆動手段)と、を主な構成要素として有している。ハウジング22は、角筒形状をなしている。また、ハウジング22の側面には、制御基板等が収容される端子箱29が設けられている。
Next, the detailed structure of the in-channel removal apparatus 6 will be described.
As shown in FIGS. 3 and 4, the in-flow channel removing device 6 has a lance tube 21 that is a tip tube inserted into the flow channel casing 4, and the tip is opened facing the denitration catalyst 3. A suction pipe 20 extending outward from the flow path casing 4, a housing 22 disposed outside the flow path casing 4 and accommodating a part of the suction pipe 20, and a drive mechanism 23 (drive means) for moving the lance tube 21 forward and backward ) As main components. The housing 22 has a rectangular tube shape. A terminal box 29 that accommodates a control board and the like is provided on the side surface of the housing 22.
 流路内除煤装置6は、流路ケーシング4の外壁4aに、ウォールボックス24を介して取り付けられている。また、流路内除煤装置6は、ランスチューブ21の長手方向(以下、単に長手方向と呼ぶ)が脱硝触媒3の端面3bに沿うように取り付けられている。 The in-flow channel removing device 6 is attached to the outer wall 4 a of the flow channel casing 4 through a wall box 24. Further, the in-flow channel removing device 6 is attached so that the longitudinal direction of the lance tube 21 (hereinafter simply referred to as the longitudinal direction) is along the end surface 3 b of the denitration catalyst 3.
 吸込管20は、ランスチューブ21と、ランスチューブ21に嵌入されたフィードパイプ25(基端管)とを有している。フィードパイプ25は、基端側、即ち長手方向においてランスチューブ21とは反対の側が塵埃配送管7を介してファン9(図1参照)と接続されている。フィードパイプ25は、基端側がハウジング22に片持ち状に支持された円管形状の部材であり、先端側が円管形状のランスチューブ21の内部に挿入されている。 The suction pipe 20 has a lance tube 21 and a feed pipe 25 (base pipe) fitted into the lance tube 21. The feed pipe 25 is connected to the fan 9 (see FIG. 1) via the dust delivery pipe 7 on the base end side, that is, the side opposite to the lance tube 21 in the longitudinal direction. The feed pipe 25 is a circular tube-shaped member whose base end side is supported in a cantilever manner on the housing 22, and a distal end side is inserted into the circular tube-shaped lance tube 21.
 ランスチューブ21は、フィードパイプ25の先端側に嵌入され、駆動機構23により長手方向に進退自在とされた円管形状の部材である。ランスチューブ21は、長手方向に沿い、フィードパイプ25と組み合わされるランスチューブ本体26と、ランスチューブ本体26の先端側に設けられている吸込管部27とから構成されている。また、ランスチューブ21は、吸込管部27を含む先端側がハウジング22の外部に突出するとともに、ウォールボックス24を貫通して、流路ケーシング4の内部に挿入されている。
 ランスチューブ本体26は、先端が流路ケーシング4の流れ方向Fに沿う方向であって、脱硝触媒3に向かう方向に曲げられており、曲げられた先の端部に吸込管部27が接続されている。
The lance tube 21 is a circular tube-shaped member that is fitted to the distal end side of the feed pipe 25 and that can be moved forward and backward in the longitudinal direction by the drive mechanism 23. The lance tube 21 is composed of a lance tube main body 26 combined with the feed pipe 25 along the longitudinal direction, and a suction pipe portion 27 provided on the distal end side of the lance tube main body 26. Further, the lance tube 21 is inserted into the flow passage casing 4 through the wall box 24 while the distal end side including the suction pipe portion 27 protrudes to the outside of the housing 22.
The lance tube main body 26 is bent in the direction along the flow direction F of the flow path casing 4 and toward the denitration catalyst 3, and the suction pipe portion 27 is connected to the bent end portion. ing.
 吸込管部27は、ランスチューブ本体26と同様に円管形状をなしており、その長手方向がランスチューブ本体26の長手方向と直交するとともに、流路ケーシング4の流れ方向Fと直交するように形成されている。即ち、吸込管部27は、脱硝触媒3の端面3bに沿うように形成されている。 The suction pipe portion 27 has a circular tube shape like the lance tube main body 26, and its longitudinal direction is orthogonal to the longitudinal direction of the lance tube main body 26 and orthogonal to the flow direction F of the flow path casing 4. Is formed. That is, the suction pipe portion 27 is formed along the end surface 3 b of the denitration catalyst 3.
 吸込管部27の両端部は閉じられている。また、吸込管部27の脱硝触媒3に対向する側には、複数の吸込口28が、吸込管部27の長手方向に沿って形成されている。吸込口28の形状は、吸込管部27の長手方向に沿う長円形状とされている。 The both ends of the suction pipe part 27 are closed. A plurality of suction ports 28 are formed along the longitudinal direction of the suction pipe portion 27 on the side of the suction pipe portion 27 facing the denitration catalyst 3. The shape of the suction port 28 is an oval shape along the longitudinal direction of the suction pipe portion 27.
 駆動機構23は、ランスチューブ21の基端に取り付けられているトラベリングキャレッジ30と、ハウジング22の外部に設けられたモータ33と、モータ33の動力をトラベリングキャレッジ30に伝達するスプロケット、チェーンを有している。 The drive mechanism 23 includes a traveling carriage 30 attached to the proximal end of the lance tube 21, a motor 33 provided outside the housing 22, and a sprocket and chain that transmits the power of the motor 33 to the traveling carriage 30. Have.
 図5に示すように、ランスチューブ21の基端には、ランスチューブ21をハウジング22の長手方向に沿って往復動自在に保持するトラベリングキャレッジ30が設けられている。トラベリングキャレッジ30は、ランスチューブ21の基端を保持するとともに、フィードパイプ25の外周を覆う形状をなしており、ランスチューブ21とフィードパイプ25との間の気密を保つ機能を有している。 As shown in FIG. 5, a traveling carriage 30 that holds the lance tube 21 in a reciprocating manner along the longitudinal direction of the housing 22 is provided at the base end of the lance tube 21. The traveling carriage 30 holds the proximal end of the lance tube 21 and has a shape covering the outer periphery of the feed pipe 25, and has a function of keeping the airtightness between the lance tube 21 and the feed pipe 25. .
 トラベリングキャレッジ30のフィードパイプ25との接触面には、トラベリングキャレッジ30の内周面とフィードパイプ25の外周面との間をシールするシール部材31が設けられている。シール部材31としては、例えばグランドパッキンを採用することができる。 A sealing member 31 that seals between the inner peripheral surface of the traveling carriage 30 and the outer peripheral surface of the feed pipe 25 is provided on the contact surface of the traveling carriage 30 with the feed pipe 25. As the sealing member 31, for example, a gland packing can be employed.
 また、トラベリングキャレッジ30には、ハウジング22の長手方向に沿って設けられているガイドレール32上を走行するガイドローラ40が取り付けられており、これにより、トラベリングキャレッジ30に保持されたランスチューブ21の長手方向に沿う移動を可能にしている。また、ガイドローラ40は、後述するリミットスイッチ45,46に当接してリミットスイッチをON/OFFすることが可能な位置に設けられている。 Further, a guide roller 40 that travels on a guide rail 32 provided along the longitudinal direction of the housing 22 is attached to the traveling carriage 30, whereby a lance tube held by the traveling carriage 30 is installed. The movement along the longitudinal direction of 21 is enabled. Further, the guide roller 40 is provided at a position where it can abut on limit switches 45 and 46, which will be described later, and turn the limit switch ON / OFF.
 ハウジング22の基端側であってハウジング22の外部には、モータ33が配置されている。このモータ33の出力軸には第一スプロケット34が取り付けられているとともに、ハウジング22の内部の基端側には第二スプロケット35が取り付けられている。第一スプロケット34と第二スプロケット35には第一チェーン36が長円軌道を形成するようにかけられている。即ち、モータ33の動力は第一スプロケット34、第一チェーン36、及び第二スプロケット35を介して、第二スプロケット35を回転可能に支持する第一回転軸37に伝達される。 A motor 33 is disposed outside the housing 22 on the base end side of the housing 22. A first sprocket 34 is attached to the output shaft of the motor 33, and a second sprocket 35 is attached to the proximal end side inside the housing 22. A first chain 36 is hung on the first sprocket 34 and the second sprocket 35 so as to form an elliptical track. That is, the power of the motor 33 is transmitted via the first sprocket 34, the first chain 36, and the second sprocket 35 to the first rotating shaft 37 that rotatably supports the second sprocket 35.
 ハウジング22の基端側に回転自在に取り付けられている第一回転軸37には、第二スプロケット35とともに回転する第三スプロケット38が取り付けられている。また、ハウジング22の先端側には、第二回転軸39が吸込管20との干渉を避けるように取り付けられており、この第二回転軸39には第四スプロケット41が回転可能に取り付けられている。第三スプロケット38と第四スプロケット41には、第二チェーン42がかけられており、これにより、第二チェーン42はハウジング22の長手方向に沿う長円軌道を形成する。
 また、第二チェーン42は、接続部材43を介してトラベリングキャレッジ30に連結されている。
A third sprocket 38 that rotates together with the second sprocket 35 is attached to a first rotating shaft 37 that is rotatably attached to the proximal end side of the housing 22. A second rotary shaft 39 is attached to the front end side of the housing 22 so as to avoid interference with the suction pipe 20, and a fourth sprocket 41 is rotatably attached to the second rotary shaft 39. Yes. A second chain 42 is hung on the third sprocket 38 and the fourth sprocket 41, whereby the second chain 42 forms an elliptical track along the longitudinal direction of the housing 22.
Further, the second chain 42 is coupled to the traveling carriage 30 via the connection member 43.
 以上のような構成により、モータ33の動力が第一回転軸37に伝達されると、第三スプロケット38が回転し、第二チェーン42がその軌道上を回転する。第二チェーン42は、トラベリングキャレッジ30に連結されているため、第二チェーン42が軌道上を走行することによって、トラベリングキャレッジ30は長手方向に沿って移動する。即ち、モータ33の動力により、トラベリングキャレッジ30と一体とされたランスチューブ21が長手方向に沿って移動する。 With the configuration as described above, when the power of the motor 33 is transmitted to the first rotating shaft 37, the third sprocket 38 rotates and the second chain 42 rotates on its track. Since the second chain 42 is connected to the traveling carriage 30, the traveling carriage 30 moves along the longitudinal direction when the second chain 42 travels on the track. That is, the lance tube 21 integrated with the traveling carriage 30 is moved along the longitudinal direction by the power of the motor 33.
 ハウジング22の先端側には逆転用リミットスイッチ45が設けられており、ハウジング22の基端側には、停止用リミットスイッチ46が設けられている。リミットスイッチ45,46は、トラベリングキャレッジ30のガイドローラ40が接触することによってスイッチが入るように配置されている。
 リミットスイッチ45,46は、ランスチューブ21及びトラベリングキャレッジ30の移動範囲の規制及び前進、後進動作を制御するようになっている。
A reverse limit switch 45 is provided on the distal end side of the housing 22, and a stop limit switch 46 is provided on the proximal end side of the housing 22. The limit switches 45 and 46 are arranged so that the switch is turned on when the guide roller 40 of the traveling carriage 30 comes into contact.
The limit switches 45 and 46 control the movement range of the lance tube 21 and the traveling carriage 30 and control the forward and reverse movements.
 ウォールボックス24は、直方体形状の箱本体47と、箱本体47の基端側に取り付けられたシールボックス48とから構成されている。箱本体47には、先端側に向く面と、その反対側の基端側を向く面にランスチューブ21が貫通する貫通孔49が形成されている。貫通孔49とランスチューブ21との間には所定の隙間が設けられている。 The wall box 24 includes a rectangular parallelepiped box body 47 and a seal box 48 attached to the base end side of the box body 47. The box body 47 is formed with a through hole 49 through which the lance tube 21 passes through a surface facing the distal end side and a surface facing the base end side opposite thereto. A predetermined gap is provided between the through hole 49 and the lance tube 21.
 シールボックス48は、直方体形状の箱状部材であり、箱本体47の基端側に設けられている。シールボックス48には、シールボックス48内を高圧に維持するための高圧シールエア供給管50が接続されている。高圧シールエア供給管50より供給されるエアは、箱本体47の基端側の貫通孔49とランスチューブ21の外周面との間の隙間を介して箱本体47に流入するようになっている。
 また、箱本体47の基端側には、取付ステー51が延在しており、ハウジング22の先端側に設けられた取付ステー52と連結されている。さらに、ハウジング22の先端側には、ランスチューブ21を下方から支持する支持ローラ53が設けられている。
The seal box 48 is a rectangular parallelepiped box-like member, and is provided on the base end side of the box body 47. The seal box 48 is connected to a high pressure seal air supply pipe 50 for maintaining the inside of the seal box 48 at a high pressure. The air supplied from the high-pressure seal air supply pipe 50 flows into the box body 47 through a gap between the through hole 49 on the base end side of the box body 47 and the outer peripheral surface of the lance tube 21.
An attachment stay 51 extends on the proximal end side of the box body 47 and is connected to an attachment stay 52 provided on the distal end side of the housing 22. Further, a support roller 53 that supports the lance tube 21 from below is provided on the front end side of the housing 22.
 次に、本実施形態に係る塵埃回収装置1の作用について説明する。
 まず、モータ33が起動すると、モータ33の回転力によって第二チェーン42が走行し、第二チェーン42に接続された接続部材43及びトラベリングキャレッジ30を介してランスチューブ21が長手方向に沿って移動する。ランスチューブ21は、逆転用リミットスイッチ45が入るまで先端側の方向に前進し、停止用リミットスイッチ46が入るまで後退するように図示しない制御装置によって制御される。
Next, the operation of the dust collection device 1 according to this embodiment will be described.
First, when the motor 33 is activated, the second chain 42 travels by the rotational force of the motor 33, and the lance tube 21 extends along the longitudinal direction via the connecting member 43 and the traveling carriage 30 connected to the second chain 42. Moving. The lance tube 21 is controlled by a control device (not shown) so as to move forward in the direction of the distal end until the reverse limit switch 45 is turned on and to move backward until the stop limit switch 46 is turned on.
 ランスチューブ21が移動する間、脱硝触媒3上の塵埃が吸引され、塵埃を含むガスがフィードパイプ25を介して塵埃配送管7に流入する。ガスの圧力は、圧力発信器14によって計測され、この圧力に応じて吸引力制御弁16が制御され、吸引力が制御される。
 また、ガスの温度は、温度発信器11によって計測され、この温度に応じて大気導入弁13が制御され、ガスの温度が制御される。
 次いで、ガスに含まれる塵埃が、バグフィルタ8によって補足され、灰処理設備へ送られる。塵埃が取り除かれたガスは、ファン9を経由して煙道に送られる。
While the lance tube 21 moves, the dust on the denitration catalyst 3 is sucked and the gas containing the dust flows into the dust delivery pipe 7 through the feed pipe 25. The pressure of the gas is measured by the pressure transmitter 14, and the suction force control valve 16 is controlled according to this pressure, and the suction force is controlled.
Further, the temperature of the gas is measured by the temperature transmitter 11, and the air introduction valve 13 is controlled according to this temperature, and the temperature of the gas is controlled.
Next, dust contained in the gas is captured by the bag filter 8 and sent to the ash treatment facility. The gas from which the dust has been removed is sent to the flue via the fan 9.
 上記実施形態によれば、脱硝触媒3に付着した塵埃、特にポップコーンアッシュのような粒径の大きな煤の塊を流路内除煤装置6の吸込管20を介して吸引して除去する構成としたため、塵埃が脱硝触媒3に堆積することを防止することができる。これにより、プラントの連続運転時間をより長くすることができる。
 また、流路ケーシング4内の塵埃が流路ケーシング4の外部に排出されるため、プラント停止時における流路ケーシング4の清掃が簡易となる。
According to the above-described embodiment, the dust adhering to the denitration catalyst 3, in particular, the lump of the soot having a large particle diameter such as popcorn ash is sucked and removed through the suction pipe 20 of the in-channel degutting device 6. Therefore, dust can be prevented from accumulating on the denitration catalyst 3. Thereby, the continuous operation time of a plant can be made longer.
Moreover, since the dust in the flow path casing 4 is discharged | emitted outside the flow path casing 4, cleaning of the flow path casing 4 at the time of a plant stop becomes easy.
 また、流路内除煤装置6によって吸引された塵埃を含むガスが、塵埃配送管7を介してバグフィルタ8に導入され、バグフィルタ8において塵埃が除去されるため、塵埃が大気に及ぶことを防止することができる。 In addition, since the gas containing dust sucked by the in-flow passage removing device 6 is introduced into the bag filter 8 through the dust delivery pipe 7, and the dust is removed by the bag filter 8, the dust reaches the atmosphere. Can be prevented.
 また、シールボックス48の内部が流路ケーシング4の内部よりも高圧に保たれていることによって、排ガスが吸込管20の挿入部より漏出することを防止することができる。 Further, since the inside of the seal box 48 is maintained at a higher pressure than the inside of the flow path casing 4, it is possible to prevent the exhaust gas from leaking out from the insertion portion of the suction pipe 20.
 また、ウォールボックス24の箱本体47の貫通孔49とランスチューブ21との間に所定の隙間を設けたことによって、排ガスの熱による外壁4aとランスチューブ21との熱膨張差による干渉を防止することができる。
 また、モータ33がハウジング22の外部に、吸込管20に対して離間して配置されていることによって、塵埃を含むガスの熱によるモータ33の損傷を防止することができる。
Further, by providing a predetermined gap between the through hole 49 of the box body 47 of the wall box 24 and the lance tube 21, interference due to the difference in thermal expansion between the outer wall 4a and the lance tube 21 due to the heat of the exhaust gas is prevented. be able to.
In addition, since the motor 33 is disposed outside the housing 22 with respect to the suction pipe 20, damage to the motor 33 due to the heat of gas containing dust can be prevented.
 なお、上記実施形態では、シールボックス48と流路ケーシング4との間に箱本体47を設ける構成としたが、ウォールボックス24の箱本体47は省略してもよい。 In the above embodiment, the box body 47 is provided between the seal box 48 and the flow path casing 4, but the box body 47 of the wall box 24 may be omitted.
(第二実施形態)
 以下、本発明の第二実施形態に係る流路内除煤装置を図面に基づいて説明する。
 図6に示すように、第二実施形態に係る流路内除煤装置6Bは、第一実施形態の流路内除煤装置6(図3参照)と比較して、吸込管20とウォールボックス24Bの構造が異なる。
(Second embodiment)
Hereinafter, an in-flow channel removal apparatus according to a second embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 6, the in-flow channel removal apparatus 6 </ b> B according to the second embodiment has a suction pipe 20 and a wall box compared to the in-flow path removal apparatus 6 (see FIG. 3) of the first embodiment. The structure of 24B is different.
 本実施形態の吸込管20Bは、駆動機構23によって長手方向に進退可能とされた移動用連動軸55と、移動用連動軸55と平行して設けられ、基端側がウォールボックス24Bに片持ち状に支持されたフィードパイプ25Bと、移動用連動軸55に平行して設けられるとともに、移動用連動軸55に接続されたランスチューブ21Bとを有している。 The suction pipe 20B of the present embodiment is provided in parallel with the moving interlocking shaft 55 that can be moved back and forth in the longitudinal direction by the drive mechanism 23, and the moving interlocking shaft 55, and the base end side is cantilevered to the wall box 24B. And a lance tube 21 </ b> B that is provided in parallel to the moving interlocking shaft 55 and connected to the moving interlocking shaft 55.
 フィードパイプ25Bの先端側はランスチューブ21Bの内部に挿入されている。移動用連動軸55は、ウォールボックス24Bを貫通して、流路ケーシング4の内部まで延在しており、その先端がランスチューブ21Bと接続されている。即ち、移動用連動軸55が進退することにより、ランスチューブ21Bが長手方向に進退するように構成されている。 The front end side of the feed pipe 25B is inserted into the lance tube 21B. The moving interlocking shaft 55 passes through the wall box 24B and extends to the inside of the flow path casing 4, and the tip thereof is connected to the lance tube 21B. That is, the lance tube 21B is configured to advance and retract in the longitudinal direction when the moving interlocking shaft 55 advances and retracts.
 ランスチューブ21Bの基端には、ランスチューブ21Bの内周面とフィードパイプ25Bの外周面との間をシールしながら、ランスチューブ21Bがフィードパイプ25B上をテレスコープ状に進退することを可能にするシール機構56が設けられている。シール機構56のフィードパイプ25Bとの接触面には、ラビリンスシール57が設けられている。 At the base end of the lance tube 21B, the lance tube 21B can advance and retreat in a telescopic manner on the feed pipe 25B while sealing between the inner peripheral surface of the lance tube 21B and the outer peripheral surface of the feed pipe 25B. A sealing mechanism 56 is provided. A labyrinth seal 57 is provided on the contact surface of the seal mechanism 56 with the feed pipe 25B.
 ランスチューブ21Bは、ランスチューブ本体26Bと、ランスチューブ本体26Bの先端に設けられた第一吸込管部58と、ランスチューブ本体の基端に設けられた第二吸込管部59とから構成されている。即ち、本実施形態のランスチューブ21Bは、2つの吸込管部58,59を有しており、第一吸込管部58が脱硝触媒3の長手方向一方側を、第二吸込管部59が脱硝触媒3の長手方向他方側を吸引するようにされている。 The lance tube 21B includes a lance tube main body 26B, a first suction pipe portion 58 provided at the tip of the lance tube main body 26B, and a second suction pipe portion 59 provided at the base end of the lance tube main body. Yes. That is, the lance tube 21B of the present embodiment has two suction pipe portions 58, 59. The first suction pipe portion 58 is on one side in the longitudinal direction of the denitration catalyst 3, and the second suction pipe portion 59 is denitration. The other side in the longitudinal direction of the catalyst 3 is sucked.
 本実施形態の流路内除煤装置6Bの作用を説明すると、モータ33の駆動により移動用連動軸55が長手方向に進退する。これにより、移動用連動軸55に連結されたランスチューブ21Bが長手方向に進退する。 Describing the operation of the in-channel removal apparatus 6B of the present embodiment, the movement interlocking shaft 55 advances and retreats in the longitudinal direction by driving the motor 33. As a result, the lance tube 21B connected to the moving interlocking shaft 55 advances and retreats in the longitudinal direction.
 上記実施形態によれば、ランスチューブ21Bによって吸引された塵埃を含むガスは、ハウジング22の内部を経由することなく、塵埃配送管7に送られるため、ガスの熱によるハウジング22内部の損傷を防止することができる。
 また、吸込管部58,59がランスチューブ21Bの先端及び基端に取り付けられているため、第一実施形態の流路内除煤装置6と比較して、ランスチューブ21Bのストロークを略半分とすることができる。
According to the above embodiment, the gas containing the dust sucked by the lance tube 21B is sent to the dust delivery pipe 7 without passing through the inside of the housing 22, so that the inside of the housing 22 is prevented from being damaged by the heat of the gas. can do.
Further, since the suction pipe portions 58 and 59 are attached to the distal end and the proximal end of the lance tube 21B, the stroke of the lance tube 21B is substantially halved as compared with the in-flow passage deguiding device 6 of the first embodiment. can do.
 図7は、流路内除煤装置の別の形態を説明する部分拡大図である。
 図7に示すように、別の形態の流路内除煤装置6Cには、脱硝触媒3の上流側に塵埃を捕捉する網である金網61が設けられている。金網61の目合は、ポップコーンアッシュのような粒径の大きい煤の塊を補足し、煤の塊の通過を阻止可能な寸法とされている。また、金網61は、脱硝触媒3の直前に配置されている。そして、ランスチューブ21の吸込口28は、金網61に対向して設けられている。
FIG. 7 is a partially enlarged view for explaining another form of the in-flow channel degreasing device.
As shown in FIG. 7, another embodiment of the in-flow passage removing apparatus 6 </ b> C is provided with a wire net 61 that is a net for capturing dust on the upstream side of the denitration catalyst 3. The mesh of the wire mesh 61 is set to a size that can complement the large lump of candy such as popcorn ash and prevent passage of the cocoon lump. Further, the wire net 61 is disposed immediately before the denitration catalyst 3. The suction port 28 of the lance tube 21 is provided to face the wire mesh 61.
 また、本実施形態の流路内除煤装置6Cのランスチューブ21には、塵埃を破砕するための破砕手段としてのブラシ62が設けられている。詳しくは、ブラシ62は、ランスチューブ本体26から先端側に突出する支持部63と、支持部63に溶接された多数の金属製のワイヤ64とから構成されており、ワイヤ64の先端が金網61に当接するように金網61及び脱硝触媒3側に突出している。 In addition, the lance tube 21 of the in-flow passage removing apparatus 6C of the present embodiment is provided with a brush 62 as a crushing means for crushing dust. Specifically, the brush 62 includes a support portion 63 that protrudes from the lance tube main body 26 toward the distal end side, and a number of metal wires 64 welded to the support portion 63, and the distal end of the wire 64 is the wire mesh 61. Projecting toward the metal mesh 61 and the denitration catalyst 3 side.
 上記形態によれば、ポップコーンアッシュのような大きな煤の塊が、金網61よりも後流側に配置された脱硝触媒3に到達することを防止することができ、プラント停止時における脱硝触媒3の清掃を容易とすることができる。
 また、ブラシ62によって粒径の大きな塵埃を破砕することによって、塵埃がより吸引されやすくなる。また、吸込口28よりも大きい塵埃を破砕することによって、より大きな塵埃を吸引することができるようになる。
According to the above embodiment, it is possible to prevent a large lump of rice cake such as popcorn ash from reaching the denitration catalyst 3 disposed on the downstream side of the wire net 61, and the denitration catalyst 3 when the plant is stopped. Cleaning can be facilitated.
Further, by crushing dust having a large particle diameter with the brush 62, the dust is more easily sucked. Further, by crushing dust larger than the suction port 28, larger dust can be sucked.
 図8は、流路内除煤装置のさらに別の形態を説明する部分拡大図であって、流れ方向Fに沿う方向から視たランスチューブ21D及び吸込管部27Dの平面図である。
 図8に示すように、本形態の流路内除煤装置6Dの吸込管部27Dには、上記各実施形態のランスチューブ本体26が接続されているとともに、塵埃除去用気体である高圧のエアを脱硝触媒3に対して吹き付けるように供給可能に構成された噴射管65を構成する第二ランスチューブ66が接続されている。
 噴射管65は吸込管20と略同様の構成を有しているが、吸込管20がファン9の吸引力によって吸込管部27Dから塵埃を吸引するのに対して、噴射管65は高圧のエアによって吸込管部27Dの吸込口28からエアを噴出させるという点で異なっている。
FIG. 8 is a partially enlarged view for explaining still another embodiment of the in-flow passage removing apparatus, and is a plan view of the lance tube 21D and the suction pipe portion 27D as viewed from the direction along the flow direction F.
As shown in FIG. 8, the lance tube main body 26 of each of the above embodiments is connected to the suction pipe portion 27D of the in-flow passage removing apparatus 6D of the present embodiment, and high-pressure air that is a dust removing gas is used. Is connected to a second lance tube 66 that constitutes an injection pipe 65 that can be supplied so as to be sprayed onto the denitration catalyst 3.
The injection pipe 65 has substantially the same configuration as the suction pipe 20, but the suction pipe 20 sucks dust from the suction pipe portion 27D by the suction force of the fan 9, whereas the injection pipe 65 has a high-pressure air. Is different in that air is ejected from the suction port 28 of the suction pipe portion 27D.
 上記形態によれば、塵埃を吸引する前の段階において、吸込管部27Dの吸込口28から高圧のエアを噴射することによって、塵埃を浮遊状態にし、その後の吸引過程において塵埃をより吸引し易くすることができる。 According to the above aspect, in a stage before sucking dust, high-pressure air is ejected from the suction port 28 of the suction pipe portion 27D to make the dust floating, and it is easier to suck dust in the subsequent suction process. can do.
 高圧のエアを供給するための形態は、これに限らず、図9に示すように、別途噴射管部67を設けて、この噴射管部67に高圧のエアを供給する噴射管65を接続する構成としてもよい。また、図9に示すように、噴射管部67は、吸込管部27Dを挟むように、2つ設ける構成としてもよい。
 また、噴射する媒体は高圧のエアに限ることはなく、例えば高圧の蒸気を噴射して粉塵を浮遊状態にする構成としてもよい。
The form for supplying high-pressure air is not limited to this, and as shown in FIG. 9, a separate injection pipe portion 67 is provided, and an injection pipe 65 for supplying high-pressure air is connected to this injection pipe portion 67. It is good also as a structure. Moreover, as shown in FIG. 9, the injection pipe part 67 is good also as a structure which provides two so that the suction pipe part 27D may be pinched | interposed.
Further, the medium to be ejected is not limited to high-pressure air, and for example, high-pressure steam may be ejected to make the dust floating.
 なお、本発明の技術範囲は上記の実施形態に限定されるものではなく、本発明の趣旨を逸脱しない範囲において、種々の変更を加えることが可能である。例えば、ガス中に含まれる塵埃を除去する方法としては、バグフィルタに限らず、粉体分離器(サイクロン)を用いてガス中の塵埃を分離してもよい。あるいは、塵埃配送管7上において、ガス中の塵埃を除去することなく、ガスをプラント内のプロセスに支障のない箇所に再度投入する構成としてもよい。
 また、上記各実施形態に係る塵埃回収装置は、吸込管で吸込み可能であれば、ポップコーンアッシュのみならず様々な大きさの塵埃を回収可能である。
The technical scope of the present invention is not limited to the above embodiment, and various modifications can be made without departing from the spirit of the present invention. For example, the method for removing the dust contained in the gas is not limited to the bag filter, and the dust in the gas may be separated using a powder separator (cyclone). Or it is good also as a structure which throws in gas again in the location which does not have trouble in the process in a plant, without removing the dust in gas on the dust delivery pipe | tube 7. FIG.
Moreover, the dust collection device according to each of the above embodiments can collect not only popcorn ash but also various sizes of dust as long as it can be sucked by the suction pipe.
 1 塵埃回収装置
 2 ボイラ
 2a 排気ダクト
 3 脱硝触媒
 4 流路ケーシング
 5 塵埃処理部
 6 流路内除煤装置
 7 塵埃配送管
 8 バグフィルタ(フィルタ)
 9 ファン(吸引手段)
 11 温度発信器
 12 温度制御装置
 13 大気導入弁
 14 圧力発信器
 15 圧力制御装置
 16 吸引力制御弁
 17 切替弁
 20 吸込管
 21 ランスチューブ(先端管)
 22 ハウジング
 23 駆動機構(駆動手段)
 24 ウォールボックス
 25 フィードパイプ(基端管)
 33 モータ
 61 金網(網)
DESCRIPTION OF SYMBOLS 1 Dust collection apparatus 2 Boiler 2a Exhaust duct 3 Denitration catalyst 4 Flow path casing 5 Dust processing part 6 Passage removal device 7 Dust delivery pipe 8 Bag filter (filter)
9 Fan (suction means)
DESCRIPTION OF SYMBOLS 11 Temperature transmitter 12 Temperature control device 13 Atmospheric introduction valve 14 Pressure transmitter 15 Pressure control device 16 Suction force control valve 17 Switching valve 20 Suction tube 21 Lance tube (tip tube)
22 Housing 23 Drive mechanism (drive means)
24 Wall box 25 Feed pipe (base pipe)
33 Motor 61 Wire mesh

Claims (10)

  1.  流体が流れる流路ケーシングに設けられ、前記流体に含まれて前記流路ケーシング内に堆積する塵埃を、前記流路ケーシング内に前記流体を流通させつつ除去するための流路内除煤装置であって、
     塵埃が除去される除去部に対向して先端が開口し、前記流路ケーシングから外側へと延びるとともに、基端側で塵埃を吸引するための吸引手段と接続される吸込管と、
     前記吸込管の開口を流路内で進退させる駆動手段とを備えることを特徴とする流路内除煤装置。
    An in-channel dedusting device for removing dust contained in the fluid and deposited in the flow channel casing while circulating the fluid in the flow channel casing. There,
    A suction pipe connected to a suction means for sucking dust on the base end side, with a distal end opening facing the removal portion from which dust is removed, extending outward from the flow path casing,
    An in-channel removal apparatus comprising driving means for advancing and retracting the opening of the suction pipe in the channel.
  2.  前記吸込管は、
     前記除去部に対向する前記開口を有する先端管と、
     基端が前記吸引手段と接続され、先端が前記先端管の内部に挿入された基端管とを有し、
     前記駆動手段は、前記先端管を進退させることを特徴とする請求項1に記載の流路内除煤装置。
    The suction pipe is
    A tip tube having the opening facing the removal portion;
    A proximal end connected to the suction means, and a distal end inserted into the distal end tube;
    2. The in-flow passage removing apparatus according to claim 1, wherein the driving means advances and retracts the tip tube.
  3.  前記駆動手段は、前記先端管及び前記基端管に沿って設けられた移動用連動軸を介して前記先端管を進退させることを特徴とする請求項2に記載の流路内除煤装置。 3. The in-flow passage removing apparatus according to claim 2, wherein the driving means advances and retracts the distal end tube via a moving interlocking shaft provided along the distal end tube and the proximal end tube.
  4.  前記流路ケーシング内の前記除去部には、塵埃を捕捉する網が設けられ、
     前記吸込管の前記開口は前記網に対向して設けられることを特徴とする請求項1から請求項3のいずれか一項に記載の流路内除煤装置。
    The removal portion in the flow path casing is provided with a net for capturing dust,
    The in-flow passage deering apparatus according to any one of claims 1 to 3, wherein the opening of the suction pipe is provided to face the net.
  5.  前記網に捕捉された塵埃を破砕する破砕手段を備えることを特徴とする請求項4に記載の流路内除煤装置。 5. The in-flow passage removing apparatus according to claim 4, further comprising a crushing means for crushing dust captured by the net.
  6.  前記除去部に塵埃除去用気体を吹き付ける吹き付け手段を備えることを特徴とする請求項1から請求項5のいずれか一項に記載の流路内除煤装置。 6. The in-flow passage removing apparatus according to claim 1, further comprising a blowing unit that blows a dust removing gas to the removing unit.
  7.  前記除去部は複数の細流路が前記流路ケーシングに沿って延在する格子状の脱硝触媒であり、前記吸込管は前記脱硝触媒の上流側に設けられていることを特徴とする請求項1から請求項6のいずれか一項に記載の流路内除煤装置。 2. The removal portion is a lattice-shaped denitration catalyst in which a plurality of narrow channels extend along the flow channel casing, and the suction pipe is provided on the upstream side of the denitration catalyst. The in-channel removal apparatus according to claim 6.
  8.  前記駆動手段を構成するモータが前記吸込管に対して離間して設けられていることを特徴とする請求項1から請求項7のいずれか一項に記載の流路内除煤装置。 8. The in-flow passage removing apparatus according to any one of claims 1 to 7, wherein a motor constituting the driving means is provided apart from the suction pipe.
  9.  請求項1から請求項8のいずれか一項に記載の流路内除煤装置と、
     前記吸込管の基端側に接続された塵埃配送管と、
     前記塵埃配送管の塵埃を捕捉するフィルタと、
     前記吸引手段とを備えることを特徴とする塵埃回収装置。
    An in-flow passage removal apparatus according to any one of claims 1 to 8,
    A dust delivery pipe connected to the proximal end side of the suction pipe;
    A filter for capturing dust in the dust delivery pipe;
    A dust collection device comprising the suction means.
  10.  前記塵埃配送管上であって、前記フィルタの上流側に冷却気体を導入する手段を備えることを特徴とする請求項9に記載の塵埃回収装置。  The dust collection device according to claim 9, further comprising means for introducing a cooling gas on the dust delivery pipe and upstream of the filter.
PCT/JP2012/063626 2012-05-28 2012-05-28 Soot removal device within flow path and dust collection device WO2013179371A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2012542285A JP5272111B1 (en) 2012-05-28 2012-05-28 Passage removal device and dust collection device
IN2148MUN2014 IN2014MN02148A (en) 2012-05-28 2012-05-28
PCT/JP2012/063626 WO2013179371A1 (en) 2012-05-28 2012-05-28 Soot removal device within flow path and dust collection device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2012/063626 WO2013179371A1 (en) 2012-05-28 2012-05-28 Soot removal device within flow path and dust collection device

Publications (1)

Publication Number Publication Date
WO2013179371A1 true WO2013179371A1 (en) 2013-12-05

Family

ID=49179195

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2012/063626 WO2013179371A1 (en) 2012-05-28 2012-05-28 Soot removal device within flow path and dust collection device

Country Status (3)

Country Link
JP (1) JP5272111B1 (en)
IN (1) IN2014MN02148A (en)
WO (1) WO2013179371A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020118392A (en) * 2019-01-25 2020-08-06 三菱日立パワーシステムズ株式会社 Dust recovery device and exhaust gas treatment device including the same and dust recovery method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109340795B (en) * 2018-09-28 2020-06-30 杭州华电江东热电有限公司 Ash removal device for waste heat boiler

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5676227A (en) * 1979-11-27 1981-06-23 Mitsubishi Heavy Ind Ltd Soot blowing method
JPH0425937U (en) * 1990-06-15 1992-03-02
JPH0473723U (en) * 1990-10-25 1992-06-29
JPH07280245A (en) * 1994-04-08 1995-10-27 Mitsubishi Heavy Ind Ltd Treating facility for burnt ash
JPH09119628A (en) * 1995-10-27 1997-05-06 Mitsubishi Heavy Ind Ltd Powdery material recovery apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5676227A (en) * 1979-11-27 1981-06-23 Mitsubishi Heavy Ind Ltd Soot blowing method
JPH0425937U (en) * 1990-06-15 1992-03-02
JPH0473723U (en) * 1990-10-25 1992-06-29
JPH07280245A (en) * 1994-04-08 1995-10-27 Mitsubishi Heavy Ind Ltd Treating facility for burnt ash
JPH09119628A (en) * 1995-10-27 1997-05-06 Mitsubishi Heavy Ind Ltd Powdery material recovery apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020118392A (en) * 2019-01-25 2020-08-06 三菱日立パワーシステムズ株式会社 Dust recovery device and exhaust gas treatment device including the same and dust recovery method
JP7171457B2 (en) 2019-01-25 2022-11-15 三菱重工業株式会社 DUST RECOVERY DEVICE, EXHAUST VACUUM PROCESSING DEVICE INCLUDING THE SAME, AND DUST COLLECTION METHOD

Also Published As

Publication number Publication date
JPWO2013179371A1 (en) 2016-01-14
JP5272111B1 (en) 2013-08-28
IN2014MN02148A (en) 2015-09-04

Similar Documents

Publication Publication Date Title
JP5392777B2 (en) Filtration dust collector
JP2011017524A (en) Method for cleaning air preheater in operating state
WO2008054107A1 (en) Apparatus for supplying compressed air using air amplifier
CN111720191B (en) DPF cleaning method and cleaning machine thereof
JP2012237242A (en) Wet exhaust gas purification device
CN214075960U (en) Lime kiln tail gas desulfurization denitration dust removal integration processing apparatus
JP5272111B1 (en) Passage removal device and dust collection device
CN106761890A (en) A kind of constructing tunnel dedusting smoke abatement secondary ventilation device
CN206027451U (en) A module is dust cleaning system in advance for catalyst regeneration project
CN113440938B (en) Dust removal and filtration device for cement kiln flue gas
JP4858727B2 (en) Flue gas denitration equipment
JP4360023B2 (en) Denitration device clogging prevention device
KR101736334B1 (en) Soot blower and method for cleaning heat exchanger
CN212583778U (en) DPF cleaning machine
TWI485356B (en) Soot blower in passage and dust recovery apparatus
KR101557314B1 (en) Rotational brush type soot removing module for selective catalytic reduction system
US20110056417A1 (en) Catalyst ash protector
JP7171457B2 (en) DUST RECOVERY DEVICE, EXHAUST VACUUM PROCESSING DEVICE INCLUDING THE SAME, AND DUST COLLECTION METHOD
CN211098177U (en) High-temperature composite filter cylinder type denitration and desulfurization dust remover
CN207493420U (en) Flue gas ultra-fine grain minimum discharge cleaning system
JP2010143659A (en) System and method for clearing hopper-clogging ash such as combustion ash
JP2005329291A (en) Filtration type dust-collector
KR101577338B1 (en) Dust collector
CN216170762U (en) Flue gas mixed structure for desulfurization and denitrification
KR101596255B1 (en) Brush type soot removing module for selective catalytic reduction system

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 2012542285

Country of ref document: JP

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12877950

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 12877950

Country of ref document: EP

Kind code of ref document: A1