WO2019022059A1 - Powder fuel burner - Google Patents

Powder fuel burner Download PDF

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Publication number
WO2019022059A1
WO2019022059A1 PCT/JP2018/027644 JP2018027644W WO2019022059A1 WO 2019022059 A1 WO2019022059 A1 WO 2019022059A1 JP 2018027644 W JP2018027644 W JP 2018027644W WO 2019022059 A1 WO2019022059 A1 WO 2019022059A1
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WO
WIPO (PCT)
Prior art keywords
powder fuel
pulverized coal
nozzle
burner
straightening
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PCT/JP2018/027644
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French (fr)
Japanese (ja)
Inventor
貴弘 小崎
誠 越前屋
恵美 大野
隆政 伊藤
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株式会社Ihi
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Publication of WO2019022059A1 publication Critical patent/WO2019022059A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel

Definitions

  • the present disclosure relates to a powder fuel burner.
  • Priority is claimed on Japanese Patent Application No. 201-143,502, filed July 25, 2017, the content of which is incorporated herein by reference.
  • a flame holder is installed between the inner center and the outer peripheral portion of the powder fuel jet hole (pulverized coal jet hole), and the flame holder is made of powder fuel (dust coal).
  • a combustion device pellet fuel burner
  • a combustion device which causes the concentrate stream to collide. In the combustion by such a powder fuel burner, a large amount of nitrogen oxides are discharged, so it is required to reduce the discharged nitrogen oxides.
  • a reduction region is formed in which the oxygen concentration is low and nitrogen oxides are reduced.
  • the powder fuel pulverized coal
  • the powder fuel spreads radially outward in response to the swirl of the transfer air and the internal circulation flow from the inside of the furnace. Therefore, the powdered fuel is not sufficiently supplied to the reduction region, and it is difficult to reduce the emission amount of nitrogen oxides.
  • the present disclosure has been made in view of the above-described problems, and aims to reduce the emission amount of nitrogen oxides by supplying a powdered fuel to a reduction region.
  • the powder fuel burner according to one aspect of the present disclosure is provided so as to stand radially inward of the nozzle portion from the inner circumferential surface of the nozzle portion that discharges air and powdered fuel along the nozzle axis, and the nozzle portion. And a powder fuel guide portion for guiding at least a part of the powder fuel flowing inside the nozzle portion radially inward.
  • the powder fuel guide portion is provided radially inward from the opening end of the nozzle portion, and a plurality of the powder fuel guide portions are arranged at intervals in the circumferential direction of the nozzle portion. It may have a current plate.
  • the powder fuel guide portion is provided on the inner peripheral surface of the nozzle portion, and protrudes toward the flow direction of the powder fuel and supports the flow straightening plate. You may have.
  • the powder fuel burner according to the above aspect may further include a gap adjusting unit configured to adjust the width of the gap between the straightening vanes.
  • the powder fuel may be pulverized coal.
  • a powder fuel guiding portion for guiding at least a part of the powder fuel flowing inside the nozzle portion radially inward.
  • the powder fuel flowing on the inner wall side of the nozzle portion can be guided radially inward, and the concentration of the powder fuel on the center side of the nozzle portion can be increased. Therefore, the powder fuel burner of the present disclosure can sufficiently supply the powdered fuel to the reduction region at the center of the flame, and can reduce the emission of nitrogen oxides.
  • FIG. 1 is a cross-sectional view including a portion of a pulverized coal burner and a furnace in accordance with an embodiment of the present disclosure. It is a front view of the baffle plate with which the pulverized coal burner in one embodiment of the present disclosure is provided. It is a perspective view which shows the support part of the baffle plate with which the pulverized coal burner in one embodiment of this indication is provided. It is a front view which shows the clearance gap adjustment part with which the pulverized coal burner in one embodiment of this indication is provided.
  • powder fuel burner using pulverized coal as a powdered fuel
  • powdered fuel is not limited to pulverized coal.
  • the powder fuel burner according to the present disclosure may be a biomass fuel burner using biomass fuel such as finely crushed wood pellets as powder fuel.
  • FIG. 1 is a cross-sectional view including a pulverized coal burner 1 (powder fuel burner) and a part of a furnace wall 100 in the present embodiment.
  • pulverized coal burner 1 pellet fuel burner
  • a furnace opening 110 communicating the inside with the outside is formed in a furnace wall 100 provided with the pulverized coal burner 1 in the present embodiment.
  • a throat is formed in the furnace opening 110 so as to expand in diameter toward the inside of the furnace wall 100.
  • the pulverized coal burner 1 is an apparatus which burns pulverized coal which is powdered coal and forms a flame inside the furnace wall 100.
  • the pulverized coal burner 1 is provided adjacent to the furnace opening 110 of the furnace wall 100, and the pulverized coal supply pipe 2 (powder fuel supply pipe), the oil gun 3, the burner nozzle 4 (nozzle portion), and air It has the supply part 5 and the pulverized coal guide part 6 (powder fuel guide part).
  • the pulverized coal supply pipe 2 is vertically connected to the burner nozzle 4 as shown in FIG.
  • the pulverized coal supply pipe 2 is connected to a pulverized coal mill (not shown), and the pulverized coal supply flow path R1 (powder fuel supply flow) which circulates in a state where the pulverized coal and the primary air are mixed in the inside of the pipe Road is formed.
  • Pulverized coal is supplied to the burner nozzle 4 via the pulverized coal supply flow path R1.
  • the oil gun 3 is a cylindrical tube formed around the nozzle axis L, and is disposed toward the furnace opening 110 of the furnace wall 100.
  • the oil gun 3 is connected to a tank (not shown) in which liquid fuel such as heavy oil or light oil is stored, and the liquid fuel flows inside.
  • the oil gun 3 discharges atomized liquid fuel toward the furnace opening 110 of the furnace wall 100 for ignition in the early stage of combustion of pulverized coal.
  • an ignition device (not shown) is provided in the vicinity of the discharge port of the oil gun 3, and the liquid fuel discharged from the oil gun 3 is ignited by the ignition device.
  • the oil gun 3 is movable along the nozzle axis L direction. Normally, the open end of the oil gun 3 is disposed so as to be inside the open end of the burner nozzle 4, and the open end of the oil gun 3 is protruded toward the furnace wall 100 when discharging liquid fuel. .
  • the burner nozzle 4 is a pipe formed concentrically with the oil gun 3 around the nozzle axis L outside the oil gun 3. Further, the opening of the burner nozzle 4 is disposed toward the furnace opening 110 of the furnace wall 100.
  • a pulverized coal discharge flow path R2 (powder fuel discharge flow path) is formed between the inner peripheral surface of the burner nozzle 4 and the outer wall surface of the oil gun 3. Pulverized coal and primary air supplied from the pulverized coal supply pipe 2 flow toward the inside of the furnace wall 100 through the pulverized coal discharge flow path R2.
  • the air supply unit 5 is a device for supplying secondary air to the flame, and has a windbox 5a, an outer throat 5b, an inner throat 5c, a main air adjusting mechanism 5d, and an auxiliary air adjusting mechanism 5e. doing.
  • the wind box 5 a is a box-like member provided outside the burner nozzle 4 and near the discharge port of the oil gun 3.
  • the secondary air is supplied to the wind box 5a in a heated state.
  • the outer throat 5 b connects the wind box 5 a and the furnace opening 110, and the diameter is reduced from the wind box 5 a toward the furnace opening 110.
  • the inner throat 5 c is a substantially annular member provided between the outer throat 5 b and the burner nozzle 4.
  • the inner throat 5 c is reduced in diameter toward the furnace opening 110.
  • an air discharge flow path R3 for supplying secondary air (air for combustion) to the furnace wall 100 is formed between the outer throat 5b and the inner throat 5c.
  • an auxiliary air discharge flow path R 4 for supplying secondary air to the furnace wall 100 is formed between the inner throat 5 c and the burner nozzle 4.
  • the main air adjustment mechanism 5d is provided upstream of the air discharge flow passage R3 and the auxiliary air discharge flow passage R4.
  • the main air adjustment mechanism 5d has a vane and a drive device such as a motor for rotating the vane, and the air flowing into the air discharge passage R3 and the auxiliary air discharge passage R4 by adjusting the direction of the vanes. Adjust the turning force of.
  • the auxiliary air adjustment mechanism 5e is provided on the upstream side of the auxiliary air discharge flow passage R4, and finely adjusts the swirling force of the secondary air flowing to the auxiliary air discharge flow passage R4 by the vanes. The swirling force of the secondary air supplied to the furnace wall 100 is adjusted by the main air adjustment mechanism 5d and the auxiliary air adjustment mechanism 5e.
  • the pulverized coal guide portion 6 has a straightening vane portion 6 a provided at an end portion of the burner nozzle 4, a support portion 6 b, and a gap adjustment portion 6 c.
  • the current plate portion 6 a is provided at an end portion of the burner nozzle 4, and an annular frame portion 6 a 1 disposed on the inner wall of the burner nozzle 4 and the frame portion 6 a 1 at the inner periphery of the frame portion 6 a 1
  • the straightening vane 6a2 is formed in a flat plate shape surrounded by two sides extending in the radial direction of the frame 6a1 and two sides in an arc shape, and is erected inward in the radial direction of the burner nozzle 4.
  • the surface of the straightening vane 6a2 which is disposed on the upstream side in the direction of pulverized coal flow is joined to the support portion 6b over the entire surface.
  • the support portion 6 b is a substantially triangular prism-shaped member provided on the upstream side of the flow direction of the pulverized coal of the flow control plate 6 a 2 of the flow control plate portion 6 a.
  • One surface of the support 6 b is joined to the straightening vane 6 a 2, and the other surface of the support 6 b is joined to the inner circumferential surface of the burner nozzle 4.
  • the support portion 6 b is disposed such that a taper is formed so as to protrude from the downstream side of the pulverized coal flow direction toward the upstream side.
  • the gap adjusting portion 6c has a movable straightening plate portion 6c1 and a projection 6c2.
  • the movable straightening plate portion 6c1 has an annular frame portion 6c3 and a ring shape having a plurality of plate portions 6c4 arranged at equal intervals to the installation intervals of the straightening vanes 6a2 of the straightening plate portion 6a on the inner periphery of the frame portion 6c3. It is a member.
  • the movable straightening vane portion 6c1 is disposed parallel to the straightening vane 6a2 on the downstream side of the flow direction of the pulverized coal with respect to the straightening vane 6a2.
  • a plurality of groove portions 6c5 are formed in an arc shape along the circumferential direction of the burner nozzle 4.
  • the protruding portion 6c2 is attached so as to protrude in the direction along the nozzle axis L from the surface of the frame portion 6a1 of the straightening vane 6a2 which is disposed on the downstream side of the pulverized coal flow direction.
  • the protrusion 6c2 is engaged with the groove 6c5 of the movable straight plate portion 6c1 and is movable along the groove 6c5.
  • the operation of the pulverized coal burner 1 having the above-described configuration will be described with reference to FIGS. 1 and 4.
  • the pulverized coal and the primary air having passed through the pulverized coal supply pipe 2 flow into the burner nozzle 4, they move toward the furnace wall 100 along the tube wall of the burner nozzle 4 inside the burner nozzle 4 and are moved to the furnace wall 100.
  • the pulverized coal supplied from the burner nozzle 4 to the furnace wall 100 is ignited in a state of being mixed with the secondary air supplied from the air supply unit 5.
  • a portion of the pulverized coal passing through the burner nozzle 4 flows along the slope (taper surface) of the support portion 6b, and is discharged to the outside from the gap between the flow straightening plates 6a2 arranged side by side.
  • the remaining pulverized coal passing through the burner nozzle 4 is guided radially inward of the burner nozzle 4 (central portion of the burner nozzle 4) by the support portion 6b and the straightening vane 6a2, and from the circular opening inside the straightening vane portion 6a. It is discharged.
  • the movable straightening plate portion 6c1 of the gap adjusting portion 6c is rotated according to the amount of combustion required in the pulverized coal burner 1, and the plate portion 6c4 of the movable straightening plate portion 6c1 is made of the straightening plate 6a2 as shown in FIG. Overlap in the gap.
  • the width of the gap between the straightening vanes 6a2 in plan view can be changed, and the flow distribution of pulverized coal at the discharge port of the burner nozzle 4 can be changed.
  • the pulverized coal guiding portion 6 is provided.
  • the flow control plate 6a2 of the pulverized coal guide portion 6 prevents the pulverized coal from collecting near the inner peripheral surface (radial direction outer side) of the burner nozzle 4 and allows the pulverized coal to flow to the central portion (radially inner side) of the burner nozzle 4 Can be guided to.
  • the pulverized coal burner 1 can reduce many nitrogen oxides in the reduction region, and can suppress the discharge amount of nitrogen oxides.
  • the pulverized coal burner 1 in the present embodiment includes a support portion 6b that supports the straightening vane 6a2 of the straightening vane portion 6a from the upstream side.
  • the support portion 6 b disperses the pressure of the pulverized coal and the primary air flowing at high speed from the upstream side toward the current plate 6 a 2 to stably support the current plate 6 a 2.
  • the support portion 6b of the present embodiment is formed into a tapered shape that protrudes toward the upstream side from the straightening vane 6a2 to reduce the resistance of the pulverized coal and the primary air, and the pulverized coal is straightened along the tapered surface. It can be guided towards the gap between each other.
  • the width of the gap between the straightening vanes 6a2 can be changed by the gap adjusting unit 6c.
  • the width of the gap between the straightening vanes 6a2 is changed between the case where it is desired to burn stably and the case where the amount of nitrogen oxide emissions is reduced, and the space is supplied to the outer region and the central region of the flame.
  • the amount (percentage) of pulverized coal can be changed.
  • the pulverized coal guide portion 6 of the pulverized coal burner 1 is configured to be provided with the gap adjusting portion 6c for adjusting the gap between the straightening vanes 6a2 of the straightening vane portion 6a, but the present disclosure is not limited thereto . It is also possible not to provide the gap adjustment part 6c. Further, the number of installed straightening vanes 6a2 of the straightening vane portion 6a and the width of the gap between the straightening vanes 6a2 can be changed according to the characteristics of the pulverized coal burner 1, the amount of combustion, and the like.
  • the support part 6b was joined to the baffle plate 6a2, and was made into the taper shape which protrudes toward the upstream side, this indication is not limited to this.
  • the support portion 6 b may be inclined radially inward and downstream in the flow direction of pulverized coal so as to guide the pulverized coal radially inward of the burner nozzle 4.
  • the straightening vane 6a2 may have a configuration in which the straightening vane 6a2 is directly joined to the burner nozzle 4 without the frame 6a1. Furthermore, the installation position of the straightening vane 6a2 is not limited to the above embodiment, and the burner nozzle 4 may be installed more upstream than the above embodiment.
  • the straightening vane 6a2 and the support portion 6b can also be integrally formed as a casting.
  • the amount of nitrogen oxide emissions can be reduced by supplying the powdered fuel to the reduction region.
  • Pulverized coal burner (powder fuel burner) 2 Pulverized coal supply piping (powder fuel supply piping) Reference Signs List 3 oil gun 4 burner nozzle 5 air supply portion 5a wind box 5b outer throat 5c inner throat 5d main air adjustment mechanism 5e auxiliary air adjustment mechanism 6 pulverized coal guide portion (powder fuel guide portion) 6a Flow straightening plate portion 6a1 Frame portion 6a2 Flow straightening plate 6b Support portion 6c Gap adjustment portion 6c1 Movable flow straightening plate portion 6c2 Projection portion 6c3 Frame portion 6c4 Plate portion 6c5 Groove portion 100 Fire wall 110 Fire wall opening

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  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

This powder fuel burner (1) comprises: a nozzle (4) that delivers air and powder fuel along a nozzle axis line; and a powder fuel guidance unit (6) that is erected on the inner circumferential face of the nozzle (4) toward the inside in the radial direction of the nozzle (4) and that guides at least some of the powder fuel flowing in the nozzle (4) toward the inside in the radial direction.

Description

粉体燃料バーナPowder fuel burner
 本開示は、粉体燃料バーナに関する。 
 本願は、2017年7月25日に日本に出願された特願2017-143502号に基づき優先権を主張し、その内容をここに援用する。
The present disclosure relates to a powder fuel burner.
Priority is claimed on Japanese Patent Application No. 201-143,502, filed July 25, 2017, the content of which is incorporated herein by reference.
 例えば、特許文献1には、粉体燃料噴出孔(微粉炭噴出孔)の内部の中心と外周部との間に保炎器を設置し、この保炎器に粉体燃料(微粉炭)の濃縮流を衝突させる燃焼装置(粉体燃料バーナ)が開示されている。このような粉体燃料バーナによる燃焼では、多量の窒素酸化物が排出されるため、排出される窒素酸化物の低減が求められている。 For example, in Patent Document 1, a flame holder is installed between the inner center and the outer peripheral portion of the powder fuel jet hole (pulverized coal jet hole), and the flame holder is made of powder fuel (dust coal). A combustion device (powder fuel burner) is disclosed which causes the concentrate stream to collide. In the combustion by such a powder fuel burner, a large amount of nitrogen oxides are discharged, so it is required to reduce the discharged nitrogen oxides.
日本国特開平8-135919号公報Japanese Patent Application Laid-Open No. 8-135919
 ところで、粉体燃料バーナにおいては、形成される火炎の中心部において、酸素濃度が低く、窒素酸化物が還元される還元領域が形成される。しかしながら、従来の粉体燃料バーナにおいては、粉体燃料(微粉炭)が、搬送空気の持つ旋回や炉内からの内部循環流を受け、径方向外側に広がる。したがって、粉体燃料が還元領域に十分に供給されず、窒素酸化物の排出量を低下させることが難しい。 By the way, in a powder fuel burner, at the center of a flame to be formed, a reduction region is formed in which the oxygen concentration is low and nitrogen oxides are reduced. However, in the conventional powder fuel burner, the powder fuel (pulverized coal) spreads radially outward in response to the swirl of the transfer air and the internal circulation flow from the inside of the furnace. Therefore, the powdered fuel is not sufficiently supplied to the reduction region, and it is difficult to reduce the emission amount of nitrogen oxides.
 本開示は、上述する問題点に鑑みてなされたもので、粉体燃料を還元領域に供給することにより窒素酸化物の排出量を低下させることを目的とする。 The present disclosure has been made in view of the above-described problems, and aims to reduce the emission amount of nitrogen oxides by supplying a powdered fuel to a reduction region.
 本開示の一態様の粉体燃料バーナは、空気と粉体燃料とをノズル軸線に沿って吐出するノズル部と、上記ノズル部の内周面からノズル部の径方向内側に向けて立設されて、ノズル部の内部を流れる粉体燃料の少なくとも一部を上記径方向内側に向けて案内する粉体燃料案内部と、を備える。 The powder fuel burner according to one aspect of the present disclosure is provided so as to stand radially inward of the nozzle portion from the inner circumferential surface of the nozzle portion that discharges air and powdered fuel along the nozzle axis, and the nozzle portion. And a powder fuel guide portion for guiding at least a part of the powder fuel flowing inside the nozzle portion radially inward.
 上記一態様の粉体燃料バーナにおいて、上記粉体燃料案内部は、上記ノズル部の開口端から径方向内側に向けて立設されると共に上記ノズル部の周方向において間隔を空けて複数配置される整流板を有していてもよい。 In the powder fuel burner according to the above aspect, the powder fuel guide portion is provided radially inward from the opening end of the nozzle portion, and a plurality of the powder fuel guide portions are arranged at intervals in the circumferential direction of the nozzle portion. It may have a current plate.
 上記一態様の粉体燃料バーナにおいて、上記粉体燃料案内部は、上記ノズル部の内周面に設けられ、粉体燃料の流れ方向に向けて突出すると共に上記整流板を支持する支持部を有していてもよい。 In the powder fuel burner of the above aspect, the powder fuel guide portion is provided on the inner peripheral surface of the nozzle portion, and protrudes toward the flow direction of the powder fuel and supports the flow straightening plate. You may have.
 上記一態様の粉体燃料バーナにおいて、上記整流板同士の間隙の幅を調整するよう構成される間隙調整部をさらに備えていてもよい。 The powder fuel burner according to the above aspect may further include a gap adjusting unit configured to adjust the width of the gap between the straightening vanes.
 上記一態様の粉体燃料バーナにおいて、上記粉体燃料が微粉炭であってもよい。 In the powder fuel burner of the above one aspect, the powder fuel may be pulverized coal.
 本開示によれば、ノズル部の内部を流れる粉体燃料の少なくとも一部を径方向内側に向けて案内する粉体燃料案内部を備えている。これにより、ノズル部の内壁側を流れる粉体燃料を径方向内側に向けて案内し、ノズル部の中心側における粉体燃料の濃度を上昇させることができる。したがって、本開示の粉体燃料バーナは、粉体燃料を火炎の中心部における還元領域に十分に供給することができ、窒素酸化物の排出量を低下させることができる。 According to the present disclosure, there is provided a powder fuel guiding portion for guiding at least a part of the powder fuel flowing inside the nozzle portion radially inward. Thus, the powder fuel flowing on the inner wall side of the nozzle portion can be guided radially inward, and the concentration of the powder fuel on the center side of the nozzle portion can be increased. Therefore, the powder fuel burner of the present disclosure can sufficiently supply the powdered fuel to the reduction region at the center of the flame, and can reduce the emission of nitrogen oxides.
本開示の一実施形態における微粉炭バーナ及び火炉の一部を含む断面図である。1 is a cross-sectional view including a portion of a pulverized coal burner and a furnace in accordance with an embodiment of the present disclosure. 本開示の一実施形態における微粉炭バーナが備える整流板の正面図である。It is a front view of the baffle plate with which the pulverized coal burner in one embodiment of the present disclosure is provided. 本開示の一実施形態における微粉炭バーナが備える整流板の支持部を示す斜視図である。It is a perspective view which shows the support part of the baffle plate with which the pulverized coal burner in one embodiment of this indication is provided. 本開示の一実施形態における微粉炭バーナが備える間隙調整部を示す正面図である。It is a front view which shows the clearance gap adjustment part with which the pulverized coal burner in one embodiment of this indication is provided.
 以下、図面を参照して、本開示に係る粉体燃料バーナの一実施形態について説明する。なお、本実施形態においては、粉体燃料バーナの一例として、粉体燃料として微粉炭を使用した微粉炭バーナについて説明する。しかしながら、粉体燃料は微粉炭に限られない。例えば、本開示に係る粉体燃料バーナは、粉体燃料として、細かく砕いた木質ペレットなどのバイオマス燃料を使用したバイオマス燃料バーナであってもよい。 Hereinafter, an embodiment of a powder fuel burner according to the present disclosure will be described with reference to the drawings. In the present embodiment, a pulverized coal burner using pulverized coal as a powdered fuel will be described as an example of the powdered fuel burner. However, powdered fuel is not limited to pulverized coal. For example, the powder fuel burner according to the present disclosure may be a biomass fuel burner using biomass fuel such as finely crushed wood pellets as powder fuel.
 図1は、本実施形態における微粉炭バーナ1(粉体燃料バーナ)及び火炉壁100の一部を含む断面図である。 FIG. 1 is a cross-sectional view including a pulverized coal burner 1 (powder fuel burner) and a part of a furnace wall 100 in the present embodiment.
 図1に示すように、本実施形態における微粉炭バーナ1が設けられる火炉壁100には、内側と外側とを連通する火炉開口110が形成されている。火炉開口110には、火炉壁100の内部へと向けて拡径するようにスロートが形成されている。 As shown in FIG. 1, a furnace opening 110 communicating the inside with the outside is formed in a furnace wall 100 provided with the pulverized coal burner 1 in the present embodiment. A throat is formed in the furnace opening 110 so as to expand in diameter toward the inside of the furnace wall 100.
 微粉炭バーナ1は、粉末状の石炭である微粉炭を燃焼させ、火炉壁100の内部に火炎を形成する装置である。微粉炭バーナ1は、火炉壁100の火炉開口110に隣接して設けられており、微粉炭供給配管2(粉体燃料供給配管)と、オイルガン3と、バーナノズル4(ノズル部)と、空気供給部5と、微粉炭案内部6(粉体燃料案内部)とを有している。 The pulverized coal burner 1 is an apparatus which burns pulverized coal which is powdered coal and forms a flame inside the furnace wall 100. The pulverized coal burner 1 is provided adjacent to the furnace opening 110 of the furnace wall 100, and the pulverized coal supply pipe 2 (powder fuel supply pipe), the oil gun 3, the burner nozzle 4 (nozzle portion), and air It has the supply part 5 and the pulverized coal guide part 6 (powder fuel guide part).
 微粉炭供給配管2は、図1に示すように、バーナノズル4に対して、垂直に接続される。微粉炭供給配管2は、不図示の微粉炭ミルと接続されており、管の内部に微粉炭と1次空気とが混合された状態で流通する微粉炭供給流路R1(粉体燃料供給流路)が形成されている。微粉炭供給流路R1を介して、バーナノズル4に微粉炭が供給される。 The pulverized coal supply pipe 2 is vertically connected to the burner nozzle 4 as shown in FIG. The pulverized coal supply pipe 2 is connected to a pulverized coal mill (not shown), and the pulverized coal supply flow path R1 (powder fuel supply flow) which circulates in a state where the pulverized coal and the primary air are mixed in the inside of the pipe Road is formed. Pulverized coal is supplied to the burner nozzle 4 via the pulverized coal supply flow path R1.
 オイルガン3は、ノズル軸線Lを中心として形成された円筒形状の管であり、火炉壁100の火炉開口110に向けて配設されている。オイルガン3は、重油または軽油等の液体燃料が貯留される不図示のタンクと接続されており、内部に液体燃料が流通する。オイルガン3は、微粉炭の燃焼初期における着火のために、火炉壁100の火炉開口110に向けて霧状の液体燃料を吐出する。また、オイルガン3の吐出口の近傍には、不図示の点火装置が設けられており、この点火装置によって、オイルガン3から吐出される液体燃料が点火される。なお、オイルガン3は、ノズル軸線L方向に沿って移動可能とされている。通常時は、オイルガン3の開口端がバーナノズル4の開口端よりも内側となるように配置され、液体燃料を吐出する際に、オイルガン3の開口端が火炉壁100に向けて突出される。 The oil gun 3 is a cylindrical tube formed around the nozzle axis L, and is disposed toward the furnace opening 110 of the furnace wall 100. The oil gun 3 is connected to a tank (not shown) in which liquid fuel such as heavy oil or light oil is stored, and the liquid fuel flows inside. The oil gun 3 discharges atomized liquid fuel toward the furnace opening 110 of the furnace wall 100 for ignition in the early stage of combustion of pulverized coal. Further, an ignition device (not shown) is provided in the vicinity of the discharge port of the oil gun 3, and the liquid fuel discharged from the oil gun 3 is ignited by the ignition device. The oil gun 3 is movable along the nozzle axis L direction. Normally, the open end of the oil gun 3 is disposed so as to be inside the open end of the burner nozzle 4, and the open end of the oil gun 3 is protruded toward the furnace wall 100 when discharging liquid fuel. .
 バーナノズル4は、オイルガン3の外側において、ノズル軸線Lを中心としてオイルガン3と同心状に形成された配管である。また、バーナノズル4の開口は、火炉壁100の火炉開口110に向けて配設されている。バーナノズル4の内周面と、オイルガン3の外壁面との間に微粉炭吐出流路R2(粉体燃料吐出流路)が形成されている。微粉炭吐出流路R2を、微粉炭供給配管2から供給される微粉炭と1次空気とが火炉壁100の内部に向かって流れる。 The burner nozzle 4 is a pipe formed concentrically with the oil gun 3 around the nozzle axis L outside the oil gun 3. Further, the opening of the burner nozzle 4 is disposed toward the furnace opening 110 of the furnace wall 100. A pulverized coal discharge flow path R2 (powder fuel discharge flow path) is formed between the inner peripheral surface of the burner nozzle 4 and the outer wall surface of the oil gun 3. Pulverized coal and primary air supplied from the pulverized coal supply pipe 2 flow toward the inside of the furnace wall 100 through the pulverized coal discharge flow path R2.
 空気供給部5は、火炎に対して2次空気を供給する装置であり、ウインドボックス5aと、外側スロート5bと、内側スロート5cと、主空気調整機構5dと、補助空気調整機構5eとを有している。ウインドボックス5aは、バーナノズル4の外側であってオイルガン3の吐出口の近傍に設けられる箱状の部材である。ウインドボックス5aには、2次空気が昇温された状態で供給される。外側スロート5bは、ウインドボックス5aと火炉開口110とを接続しており、ウインドボックス5aから火炉開口110に向けて縮径されている。 The air supply unit 5 is a device for supplying secondary air to the flame, and has a windbox 5a, an outer throat 5b, an inner throat 5c, a main air adjusting mechanism 5d, and an auxiliary air adjusting mechanism 5e. doing. The wind box 5 a is a box-like member provided outside the burner nozzle 4 and near the discharge port of the oil gun 3. The secondary air is supplied to the wind box 5a in a heated state. The outer throat 5 b connects the wind box 5 a and the furnace opening 110, and the diameter is reduced from the wind box 5 a toward the furnace opening 110.
 内側スロート5cは、外側スロート5bとバーナノズル4の間に設けられた略円環状の部材である。内側スロート5cは火炉開口110に向けて縮径されている。また、外側スロート5bと、内側スロート5cとの間には、火炉壁100へと2次空気(燃焼用空気)を供給する空気吐出流路R3が形成される。また、内側スロート5cとバーナノズル4との間には、火炉壁100へと2次空気を供給する補助空気吐出流路R4が形成される。 The inner throat 5 c is a substantially annular member provided between the outer throat 5 b and the burner nozzle 4. The inner throat 5 c is reduced in diameter toward the furnace opening 110. Further, an air discharge flow path R3 for supplying secondary air (air for combustion) to the furnace wall 100 is formed between the outer throat 5b and the inner throat 5c. In addition, between the inner throat 5 c and the burner nozzle 4, an auxiliary air discharge flow path R 4 for supplying secondary air to the furnace wall 100 is formed.
 主空気調整機構5dは、空気吐出流路R3及び補助空気吐出流路R4の上流に設けられている。主空気調整機構5dは、ベーンと、ベーンを回動させるモータ等の駆動装置を有し、ベーンの向きを調整することにより、空気吐出流路R3及び補助空気吐出流路R4へと流入する空気の旋回力を調節する。補助空気調整機構5eは、補助空気吐出流路R4の上流側に設けられており、ベーンにより補助空気吐出流路R4へと流れる2次空気の旋回力を微調節する。主空気調整機構5d及び補助空気調整機構5eにより、火炉壁100へと供給される2次空気の旋回力が調整される。 The main air adjustment mechanism 5d is provided upstream of the air discharge flow passage R3 and the auxiliary air discharge flow passage R4. The main air adjustment mechanism 5d has a vane and a drive device such as a motor for rotating the vane, and the air flowing into the air discharge passage R3 and the auxiliary air discharge passage R4 by adjusting the direction of the vanes. Adjust the turning force of. The auxiliary air adjustment mechanism 5e is provided on the upstream side of the auxiliary air discharge flow passage R4, and finely adjusts the swirling force of the secondary air flowing to the auxiliary air discharge flow passage R4 by the vanes. The swirling force of the secondary air supplied to the furnace wall 100 is adjusted by the main air adjustment mechanism 5d and the auxiliary air adjustment mechanism 5e.
 微粉炭案内部6は、バーナノズル4の端部に設けられる整流板部6aと、支持部6bと、間隙調整部6cとを有している。整流板部6aは、図2に示すように、バーナノズル4の端部に設けられ、バーナノズル4の内壁に配置される円環状の枠部6a1と、枠部6a1の内周において、枠部6a1に平行かつバーナノズル4の周方向において等間隔となるように配列される複数(本実施形態においては10枚)の整流板6a2とを有する櫛歯状の環状部材である。
 整流板6a2は、枠部6a1の径方向に向かう2辺と、円弧状の2辺とに囲まれた平板状とされ、バーナノズル4の径方向内側に向けて立設される。整流板6a2の微粉炭流動方向上流側に配置される面が全面において支持部6bと接合されている。
The pulverized coal guide portion 6 has a straightening vane portion 6 a provided at an end portion of the burner nozzle 4, a support portion 6 b, and a gap adjustment portion 6 c. As shown in FIG. 2, the current plate portion 6 a is provided at an end portion of the burner nozzle 4, and an annular frame portion 6 a 1 disposed on the inner wall of the burner nozzle 4 and the frame portion 6 a 1 at the inner periphery of the frame portion 6 a 1 It is a comb-like annular member having a plurality of (in this embodiment, 10) flow straightening plates 6a2 arranged in parallel and at equal intervals in the circumferential direction of the burner nozzle 4.
The straightening vane 6a2 is formed in a flat plate shape surrounded by two sides extending in the radial direction of the frame 6a1 and two sides in an arc shape, and is erected inward in the radial direction of the burner nozzle 4. The surface of the straightening vane 6a2 which is disposed on the upstream side in the direction of pulverized coal flow is joined to the support portion 6b over the entire surface.
 支持部6bは、図3に示すように、整流板部6aの整流板6a2の微粉炭流動方向上流側に各々設けられた略三角柱状の部材である。支持部6bの一面が整流板6a2と接合され、また支持部6bの他の一面がバーナノズル4の内周面と接合されている。支持部6bは、微粉炭流動方向下流側から上流側に向けて突出するテーパが形成されるように配置される。これにより、整流板6a2を上流側から安定的に支持すると共に、微粉炭及び1次空気の整流板部6aによる抵抗を低減し、微粉炭が整流板6a2の内側に堆積することを防止している。 As shown in FIG. 3, the support portion 6 b is a substantially triangular prism-shaped member provided on the upstream side of the flow direction of the pulverized coal of the flow control plate 6 a 2 of the flow control plate portion 6 a. One surface of the support 6 b is joined to the straightening vane 6 a 2, and the other surface of the support 6 b is joined to the inner circumferential surface of the burner nozzle 4. The support portion 6 b is disposed such that a taper is formed so as to protrude from the downstream side of the pulverized coal flow direction toward the upstream side. Thereby, while stably supporting the straightening vane 6a2 from the upstream side, the resistance of the pulverized coal and the primary air by the straightening vane portion 6a is reduced, and the pulverized coal is prevented from being deposited inside the straightening vane 6a2. There is.
 間隙調整部6cは、図4に示すように、可動整流板部6c1と、突起部6c2とを有している。可動整流板部6c1は、円環状の枠部6c3と、枠部6c3の内周において、整流板部6aの整流板6a2の設置間隔と等しい間隔で配置された複数の板部6c4とを有する環状部材である。可動整流板部6c1は、整流板6a2よりも微粉炭の流動方向下流側において、整流板6a2と平行に配置される。枠部6c3には、複数の溝部6c5がバーナノズル4の周方向に沿った円弧状に形成されている。突起部6c2は、整流板6a2の枠部6a1の微粉炭流動方向下流側に配置される面からノズル軸線Lに沿う方向に突出して取り付けられる。突起部6c2は、可動整流板部6c1の溝部6c5に係合しており、溝部6c5に沿って移動可能となっている。 As shown in FIG. 4, the gap adjusting portion 6c has a movable straightening plate portion 6c1 and a projection 6c2. The movable straightening plate portion 6c1 has an annular frame portion 6c3 and a ring shape having a plurality of plate portions 6c4 arranged at equal intervals to the installation intervals of the straightening vanes 6a2 of the straightening plate portion 6a on the inner periphery of the frame portion 6c3. It is a member. The movable straightening vane portion 6c1 is disposed parallel to the straightening vane 6a2 on the downstream side of the flow direction of the pulverized coal with respect to the straightening vane 6a2. In the frame portion 6c3, a plurality of groove portions 6c5 are formed in an arc shape along the circumferential direction of the burner nozzle 4. The protruding portion 6c2 is attached so as to protrude in the direction along the nozzle axis L from the surface of the frame portion 6a1 of the straightening vane 6a2 which is disposed on the downstream side of the pulverized coal flow direction. The protrusion 6c2 is engaged with the groove 6c5 of the movable straight plate portion 6c1 and is movable along the groove 6c5.
 続いて、上記構成の微粉炭バーナ1の作用について、図1及び図4を参照して説明する。
 微粉炭供給配管2を通過した微粉炭及び1次空気は、バーナノズル4に流入すると、バーナノズル4の内部において、バーナノズル4の管壁に沿って、火炉壁100に向けて移動し、火炉壁100に供給される。バーナノズル4から火炉壁100に供給された微粉炭は、空気供給部5から供給される2次空気と混合された状態で着火する。
Subsequently, the operation of the pulverized coal burner 1 having the above-described configuration will be described with reference to FIGS. 1 and 4.
When the pulverized coal and the primary air having passed through the pulverized coal supply pipe 2 flow into the burner nozzle 4, they move toward the furnace wall 100 along the tube wall of the burner nozzle 4 inside the burner nozzle 4 and are moved to the furnace wall 100. Supplied. The pulverized coal supplied from the burner nozzle 4 to the furnace wall 100 is ignited in a state of being mixed with the secondary air supplied from the air supply unit 5.
 バーナノズル4を通過する微粉炭の一部は、支持部6bの傾斜(テーパ面)に沿って流れ、並んで配置された整流板6a2同士の間隙から外側に吐出される。また、バーナノズル4を通過する残りの微粉炭は、支持部6b及び整流板6a2によりバーナノズル4の径方向内側(バーナノズル4の中央部)に向けて案内され、整流板部6aの内側の円形開口から吐出される。 A portion of the pulverized coal passing through the burner nozzle 4 flows along the slope (taper surface) of the support portion 6b, and is discharged to the outside from the gap between the flow straightening plates 6a2 arranged side by side. The remaining pulverized coal passing through the burner nozzle 4 is guided radially inward of the burner nozzle 4 (central portion of the burner nozzle 4) by the support portion 6b and the straightening vane 6a2, and from the circular opening inside the straightening vane portion 6a. It is discharged.
 また、微粉炭バーナ1において必要な燃焼量に応じて、間隙調整部6cの可動整流板部6c1を回転させ、図4に示すように、可動整流板部6c1の板部6c4を整流板6a2の隙間に重ね合わせる。これにより、平面視における整流板6a2同士の間隙の幅を変更することができ、バーナノズル4の吐出口における微粉炭の流量分布を変えることができる。整流板6a2同士の間隙の幅を狭くすると、バーナノズル4の内壁の近傍における微粉炭の量がより低くなり、バーナノズル4の中央部における微粉炭の濃度がより高くなる。 Further, the movable straightening plate portion 6c1 of the gap adjusting portion 6c is rotated according to the amount of combustion required in the pulverized coal burner 1, and the plate portion 6c4 of the movable straightening plate portion 6c1 is made of the straightening plate 6a2 as shown in FIG. Overlap in the gap. Thus, the width of the gap between the straightening vanes 6a2 in plan view can be changed, and the flow distribution of pulverized coal at the discharge port of the burner nozzle 4 can be changed. When the width of the gap between the straightening vanes 6a2 is narrowed, the amount of pulverized coal in the vicinity of the inner wall of the burner nozzle 4 becomes lower, and the concentration of pulverized coal in the central portion of the burner nozzle 4 becomes higher.
 このような本実施形態における微粉炭バーナ1によれば、微粉炭案内部6を備えている。微粉炭案内部6の整流板6a2により、微粉炭がバーナノズル4の内周面の近傍(径方向外側)に集まることを防止し、微粉炭をバーナノズル4の中央部(径方向内側)に流れるように案内することができる。これにより、バーナノズル4から微粉炭が吐出される際に、火炎の中心部に形成された還元領域に微粉炭を多く供給することができる。したがって、微粉炭バーナ1は、還元領域において窒素酸化物を多く還元することができ、窒素酸化物の排出量を抑制することができる。 According to the pulverized coal burner 1 in the present embodiment, the pulverized coal guiding portion 6 is provided. The flow control plate 6a2 of the pulverized coal guide portion 6 prevents the pulverized coal from collecting near the inner peripheral surface (radial direction outer side) of the burner nozzle 4 and allows the pulverized coal to flow to the central portion (radially inner side) of the burner nozzle 4 Can be guided to. Thus, when the pulverized coal is discharged from the burner nozzle 4, a large amount of pulverized coal can be supplied to the reduction region formed in the center of the flame. Therefore, the pulverized coal burner 1 can reduce many nitrogen oxides in the reduction region, and can suppress the discharge amount of nitrogen oxides.
 また、本実施形態における微粉炭バーナ1は、整流板部6aの整流板6a2を上流側から支持する支持部6bを備えている。支持部6bは、上流側から整流板6a2に向けて高速で流れる微粉炭及び1次空気の圧力を分散させて整流板6a2を安定的に支持している。また、本実施形態の支持部6bは、整流板6a2から上流側に向けて突出するテーパ状とされ、微粉炭及び1次空気の抵抗を低減し、微粉炭をテーパ面に沿って整流板6a2同士の間隙に向けて案内することができる。 In addition, the pulverized coal burner 1 in the present embodiment includes a support portion 6b that supports the straightening vane 6a2 of the straightening vane portion 6a from the upstream side. The support portion 6 b disperses the pressure of the pulverized coal and the primary air flowing at high speed from the upstream side toward the current plate 6 a 2 to stably support the current plate 6 a 2. Further, the support portion 6b of the present embodiment is formed into a tapered shape that protrudes toward the upstream side from the straightening vane 6a2 to reduce the resistance of the pulverized coal and the primary air, and the pulverized coal is straightened along the tapered surface. It can be guided towards the gap between each other.
 さらに、本実施形態における微粉炭バーナ1によれば、間隙調整部6cにより、整流板6a2同士の間隙の幅を変更することができる。これにより、安定的に燃焼させたい場合と、窒素酸化物の排出量を低下させたい場合とで、整流板6a2同士の間隙の幅を変更させ、火炎の外側領域と中心領域とに供給される微粉炭の量(割合)を変更することができる。 Furthermore, according to the pulverized coal burner 1 in the present embodiment, the width of the gap between the straightening vanes 6a2 can be changed by the gap adjusting unit 6c. As a result, the width of the gap between the straightening vanes 6a2 is changed between the case where it is desired to burn stably and the case where the amount of nitrogen oxide emissions is reduced, and the space is supplied to the outer region and the central region of the flame. The amount (percentage) of pulverized coal can be changed.
 以上、図面を参照しながら本開示の好適な実施形態について説明したが、本開示は上記実施形態に限定されるものではない。上述した実施形態において示した各構成部材の諸形状や組み合わせ等は一例であって、本開示の趣旨から逸脱しない範囲において設計要求等に基づき種々変更可能である。 The preferred embodiments of the present disclosure have been described above with reference to the drawings, but the present disclosure is not limited to the above-described embodiments. The shapes, combinations, and the like of the constituent members shown in the above-described embodiment are merely examples, and various changes can be made based on design requirements and the like without departing from the spirit of the present disclosure.
 上記実施形態においては、微粉炭バーナ1の微粉炭案内部6は、整流板部6aの整流板6a2同士の間隙を調整する間隙調整部6cを設ける構成としたが、本開示はこれに限定されない。間隙調整部6cを設けない構成とすることも可能である。また、整流板部6aの整流板6a2の設置数及び整流板6a2同士の間隙の幅は、微粉炭バーナ1の特性や、燃焼量等に応じて変更可能である。 In the above embodiment, the pulverized coal guide portion 6 of the pulverized coal burner 1 is configured to be provided with the gap adjusting portion 6c for adjusting the gap between the straightening vanes 6a2 of the straightening vane portion 6a, but the present disclosure is not limited thereto . It is also possible not to provide the gap adjustment part 6c. Further, the number of installed straightening vanes 6a2 of the straightening vane portion 6a and the width of the gap between the straightening vanes 6a2 can be changed according to the characteristics of the pulverized coal burner 1, the amount of combustion, and the like.
 また、上記実施形態においては、支持部6bは、整流板6a2に接合され、上流側に向けて突出するテーパ状とされたが、本開示はこれに限定されない。支持部6bは、バーナノズル4の径方向内側に向けて微粉炭を案内するように、径方向内側かつ微粉炭流動方向下流側に向けて傾斜した形状としてもよい。 Moreover, in the said embodiment, although the support part 6b was joined to the baffle plate 6a2, and was made into the taper shape which protrudes toward the upstream side, this indication is not limited to this. The support portion 6 b may be inclined radially inward and downstream in the flow direction of pulverized coal so as to guide the pulverized coal radially inward of the burner nozzle 4.
 また、整流板6a2は、枠部6a1を有さず、バーナノズル4に直接整流板6a2が接合される構成とすることも可能である。さらに、整流板6a2の設置位置は上記実施形態に限定されず、バーナノズル4において、上記実施形態よりも、より上流側に設置することも可能である。 The straightening vane 6a2 may have a configuration in which the straightening vane 6a2 is directly joined to the burner nozzle 4 without the frame 6a1. Furthermore, the installation position of the straightening vane 6a2 is not limited to the above embodiment, and the burner nozzle 4 may be installed more upstream than the above embodiment.
 また、整流板6a2と支持部6bとは、鋳物として一体形成することも可能である。 The straightening vane 6a2 and the support portion 6b can also be integrally formed as a casting.
 本開示によれば、粉体燃料を還元領域に供給することにより窒素酸化物の排出量を低下させることができる。 According to the present disclosure, the amount of nitrogen oxide emissions can be reduced by supplying the powdered fuel to the reduction region.
1 微粉炭バーナ(粉体燃料バーナ)
2 微粉炭供給配管(粉体燃料供給配管)
3 オイルガン
4 バーナノズル
5 空気供給部
5a ウインドボックス
5b 外側スロート
5c 内側スロート
5d 主空気調整機構
5e 補助空気調整機構
6 微粉炭案内部(粉体燃料案内部)
6a 整流板部
6a1 枠部
6a2 整流板
6b 支持部
6c 間隙調整部
6c1 可動整流板部
6c2 突起部
6c3 枠部
6c4 板部
6c5 溝部
100 火炉壁
110 火炉開口
1 Pulverized coal burner (powder fuel burner)
2 Pulverized coal supply piping (powder fuel supply piping)
Reference Signs List 3 oil gun 4 burner nozzle 5 air supply portion 5a wind box 5b outer throat 5c inner throat 5d main air adjustment mechanism 5e auxiliary air adjustment mechanism 6 pulverized coal guide portion (powder fuel guide portion)
6a Flow straightening plate portion 6a1 Frame portion 6a2 Flow straightening plate 6b Support portion 6c Gap adjustment portion 6c1 Movable flow straightening plate portion 6c2 Projection portion 6c3 Frame portion 6c4 Plate portion 6c5 Groove portion 100 Fire wall 110 Fire wall opening

Claims (5)

  1.  空気と粉体燃料とをノズル軸線に沿って吐出するノズル部と、
     前記ノズル部の内周面から前記ノズル部の径方向内側に向けて立設されて、前記ノズル部の内部を流れる粉体燃料の少なくとも一部を前記径方向内側に向けて案内する粉体燃料案内部と、
    を備える粉体燃料バーナ。
    A nozzle unit that discharges air and powdered fuel along a nozzle axis;
    Powder fuel that is erected radially inward of the nozzle portion from an inner peripheral surface of the nozzle portion, and guides at least a portion of the powder fuel flowing inside the nozzle portion in the radial direction A guidance unit,
    Powder fuel burner comprising.
  2.  前記粉体燃料案内部は、前記ノズル部の開口端から前記径方向内側に向けて立設されると共に前記ノズル部の周方向において間隔を空けて複数配置される整流板を有する請求項1記載の粉体燃料バーナ。 The powder fuel guide portion has straightening vanes erected inward in the radial direction from the opening end of the nozzle portion and provided with a plurality of flow guide plates spaced apart in the circumferential direction of the nozzle portion. Powder fuel burner.
  3.  前記粉体燃料案内部は、前記ノズル部の内周面に設けられ、粉体燃料の流れ方向に向けて突出すると共に前記整流板を支持する支持部を有する請求項2記載の粉体燃料バーナ。 The powder fuel burner according to claim 2, wherein the powder fuel guide portion is provided on an inner peripheral surface of the nozzle portion, and has a support portion protruding in the flow direction of the powder fuel and supporting the straightening vane. .
  4.  前記整流板同士の間隙の幅を調整するよう構成される間隙調整部をさらに備える請求項2または3記載の粉体燃料バーナ。 The powder fuel burner according to claim 2 or 3, further comprising a gap adjusting unit configured to adjust a width of a gap between the straightening vanes.
  5.  前記粉体燃料が微粉炭である請求項1~4のいずれか一項に記載の粉体燃料バーナ。 The powder fuel burner according to any one of claims 1 to 4, wherein the powder fuel is pulverized coal.
PCT/JP2018/027644 2017-07-25 2018-07-24 Powder fuel burner WO2019022059A1 (en)

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JP2017143502 2017-07-25
JP2017-143502 2017-07-25

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Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS599002B2 (en) * 1977-01-11 1984-02-28 バブコツク日立株式会社 Pulverized coal combustion method
JPS63116715U (en) * 1987-01-14 1988-07-28
JPH01305206A (en) * 1988-03-04 1989-12-08 Northern Eng Ind Plc Burner
JPH04214102A (en) * 1990-03-07 1992-08-05 Hitachi Ltd Pulverized coal boiler, pulverized coal boiler system, and pulverized coal burner
JPH10220707A (en) * 1997-02-10 1998-08-21 Babcock Hitachi Kk Burner for powdery solid fuel and combustion apparatus therewith
US5799594A (en) * 1993-11-08 1998-09-01 Ivo International Oy Method and apparatus for reducing nitrogen oxide emissions from burning pulverized fuel
JP2000130710A (en) * 1998-10-27 2000-05-12 Hitachi Ltd Pulverized coal combustion burner
JP2010270992A (en) * 2009-05-22 2010-12-02 Mitsubishi Heavy Ind Ltd Coal burning boiler
JP4969015B2 (en) * 2000-08-04 2012-07-04 バブコック日立株式会社 Solid fuel burner and combustion method using solid fuel burner
JP2012255600A (en) * 2011-06-09 2012-12-27 Babcock Hitachi Kk Solid fuel burner and combustion device including the same
JP2014173777A (en) * 2013-03-07 2014-09-22 Mitsubishi Heavy Ind Ltd Combustion burner and boiler
JP2016133224A (en) * 2015-01-15 2016-07-25 三菱日立パワーシステムズ株式会社 Solid fuel burner

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS599002B2 (en) * 1977-01-11 1984-02-28 バブコツク日立株式会社 Pulverized coal combustion method
JPS63116715U (en) * 1987-01-14 1988-07-28
JPH01305206A (en) * 1988-03-04 1989-12-08 Northern Eng Ind Plc Burner
JPH04214102A (en) * 1990-03-07 1992-08-05 Hitachi Ltd Pulverized coal boiler, pulverized coal boiler system, and pulverized coal burner
US5799594A (en) * 1993-11-08 1998-09-01 Ivo International Oy Method and apparatus for reducing nitrogen oxide emissions from burning pulverized fuel
JPH10220707A (en) * 1997-02-10 1998-08-21 Babcock Hitachi Kk Burner for powdery solid fuel and combustion apparatus therewith
JP2000130710A (en) * 1998-10-27 2000-05-12 Hitachi Ltd Pulverized coal combustion burner
JP4969015B2 (en) * 2000-08-04 2012-07-04 バブコック日立株式会社 Solid fuel burner and combustion method using solid fuel burner
JP2010270992A (en) * 2009-05-22 2010-12-02 Mitsubishi Heavy Ind Ltd Coal burning boiler
JP2012255600A (en) * 2011-06-09 2012-12-27 Babcock Hitachi Kk Solid fuel burner and combustion device including the same
JP2014173777A (en) * 2013-03-07 2014-09-22 Mitsubishi Heavy Ind Ltd Combustion burner and boiler
JP2016133224A (en) * 2015-01-15 2016-07-25 三菱日立パワーシステムズ株式会社 Solid fuel burner

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