JP3746642B2 - Pulverized coal concentration adjustment device - Google Patents

Pulverized coal concentration adjustment device Download PDF

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Publication number
JP3746642B2
JP3746642B2 JP25100899A JP25100899A JP3746642B2 JP 3746642 B2 JP3746642 B2 JP 3746642B2 JP 25100899 A JP25100899 A JP 25100899A JP 25100899 A JP25100899 A JP 25100899A JP 3746642 B2 JP3746642 B2 JP 3746642B2
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Prior art keywords
pulverized coal
concentration
pipe
pulverized
inclined surface
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JP2001074236A (en
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勇俊 榮
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Mitsubishi Heavy Industries Ltd
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Mitsubishi Heavy Industries Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、微粉炭燃焼ボイラの火炉に取付けられたバーナへ微粉炭を供給する微粉炭管内の微粉炭濃度調整装置に関する。
【0002】
【従来の技術】
微粉炭燃焼ボイラの火炉には、複数本の微粉炭バーナが取付けられており、2本のバーナに対してはそれぞれ1基の1次分配器が設けられている。この1次分配器は、石炭ミル付近の利用スペースが少なく、微粉炭管(ダクト)の配管の複雑化を防止したり、材料費を低減させるなどの観点から、2本のバーナに対して1本の微粉炭管を共用できるようにするために設けられている。
【0003】
上記1次分配器としては、例えば、図5に示すようなものがある。この1次分配器51は、微粉炭52が空気により送られて矢印A方向へ流れる微粉炭管53と、下流側の位置で左右両側に分岐する分岐管54,55とにそれぞれ接続されており、その内部には、複数枚の仕切板56で仕切られた複数段の流路が上下左右にわたって形成されている。これら各段の流路の下流端には、盲板57が上下方向で左右交互に配設され、同盲板57によって分岐管54,55の一方との連通を遮断しており、これら分岐管54,55内には、左右に分割された流れ(矢印B方向、C方向)で微粉炭52が気送されるようになっている。
【0004】
すなわち、図示しない石炭ミルで粉砕された微粉炭52は、複数本の微粉炭管53を通って1次分配器51に空気輸送されると共に、同1次分配器51の各流路からそれぞれ分岐管54,55を経て火炉に設けた複数本のバーナ(図示せず)へ供給され、同バーナで燃焼されることになる。
【0005】
【発明が解決しようとする課題】
しかしながら、微粉炭管53内を空気輸送される微粉炭52は、空気と比べて質量が大きく、重力沈降する傾向にあるので、微粉炭管53の下部を流れる微粉炭52の濃度が高く、1次分配器51の入口において上下方向の濃度分布が不均一となり、同1次分配器51の各流路から左右の分岐管54,55を経て各バーナへ供給される微粉炭52の配分に差異が生じ、NOx・未燃分の増加を招く恐れがある。
【0006】
本発明はこのような実状に鑑みてなされたものであって、その目的は、1次分配器の入口における上下方向の濃度分布を改善し、各バーナへの微粉炭配分の均一化を図ることが可能な微粉炭濃度調整装置を提供することにある。
【0007】
【課題を解決するための手段】
上記従来技術の有する課題を達成するために、本発明は、微粉炭が気送されて流れる微粉炭管に接続されると共に、下流側の複数の分岐管に接続され、上下左右にわたって形成された複数段の流路より前記微粉炭を各分岐管に分配して気送する1次分配器を備え、該1次分配器の上流側で前記微粉炭管内の下部に、前記分岐管への微粉炭濃度を調整する固気二相流調整手段を設けた微粉炭濃度調整装置であって、前記固気二相流調整手段は、前記微粉炭管の全巾に沿って設けられ、かつ上面が前記微粉炭の流れの方向に対して徐々に立ち上がる傾斜面を備えたキッカブロックであり、該キッカブロックは、前記微粉炭管内の下部を流れる微粉炭の濃度に応じて傾斜面の角度が調整可能に構成されている。
【0008】
また、本発明では、前記キッカブロックの傾斜面に、耐摩耗材が設けられている。
【0009】
【発明の実施の形態】
以下、本発明を図示の実施の形態に基づいて詳細に説明する。ここで、図1は本発明の実施の形態に係る微粉炭濃度調整装置が適用される1次分配器の取付位置の概念図、図2は本実施の形態に係る微粉炭濃度調整装置及び1次分配器の設置付近の斜視図、図3は図2の微粉炭濃度調整装置を設けた微粉炭管内を流れる微粉炭の分散状態の概念図、図4は本実施の形態の微粉炭濃度調整装置による改善効果確認試験結果の線図を示している。
【0010】
本発明の実施の形態に係る微粉炭濃度調整装置が適用される微粉炭燃焼ボイラは、図1〜図3に示す如く、供給された微粉炭1を微粉炭バーナ2で燃焼させて熱を発生させる火炉3と、同火炉3の上方に所定のピッチで並列配置され、内部に蒸気を流し外部から燃焼熱を伝えて熱し、所定の圧力及び温度の蒸気を発生させる伝熱管群(図示せず)とを備えており、同微粉炭燃焼ボイラから出た燃焼ガスは、図示しない空気予熱器や電気集塵器等を介して煙突から排出されるように構成されている。
また、上記微粉炭燃焼ボイラと関連して、供給された石炭を粉砕することにより微粉炭1を製造する石炭ミル4が設備されており、同微粉炭1は、空気輸送によって石炭ミル4から4本の微粉炭管5a〜5d内を通り、4基の1次分配器6a〜6d及び各分岐管7,8を経て、火炉3の外周に所定の間隔を置いて取付けた8本の微粉炭バーナ2a〜2hのそれぞれに供給されるようになっている。
【0011】
上記1次分配器6a〜6dは、従来と同様の構造を有し、微粉炭1が空気により送られて矢印A方向へ流れる微粉炭管5a〜5dと、下流側の位置で左右両側に分岐する分岐管7,8とにそれぞれ接続されており、その内部には、複数枚の仕切板9で仕切られた複数段の流路10が上下左右にわたって形成されている。これら各段の流路10の下流端側には、盲板11が上下方向で左右交互に配設され、同盲板11によって分岐管7,8の一方との連通を遮断しており、これら分岐管7,8内には、矢印B方向と矢印C方向へ左右に分割された流れで微粉炭1が気送されるようになっている。
【0012】
また、上記1次分配器6a〜6dの入口の上流側であって、微粉炭管5a〜5d内の下部には、図2及び図3に示す如く、下流側に位置する左右両側の分岐管7,8への微粉炭濃度を調整する固気二相流調整手段のキッカブロック12が設けられている。このキッカブロック12は、本発明の実施の形態に係る微粉炭濃度調整装置を構成するもので、微粉炭管5a〜5dの全巾に沿って設けられており、その上面は、微粉炭1の流れの方向(矢印A方向)に対して徐々に立ち上がる角度θの傾斜面12aを備えている。すなわち、キッカブロック12は、傾斜面12aにより下流側(1次分配器6a〜6dの入口側)が高くなっており、側方から見て断面略三角形状に形成されている。なお、図3において符号Dは微粉炭管5a〜5d内の微粉炭濃度分布を示している。
【0013】
しかも、上記キッカブロック12は、公知の高さ位置変更手段等を用いることにより、微粉炭管5a〜5dの下部を流れる微粉炭1の濃度などに応じて、傾斜面12aの角度θが調整可能に構成されている。この角度θの調整作業は、通常、装置完成後の試験運転時に行われており、左右両側の分岐管7,8への微粉炭濃度を変更調整することによって、運転時における各バーナ2a〜2hへの微粉炭1の配分が均一になされている。
また、キッカブロック12の傾斜面12aには、通過していく微粉炭1による摩耗を防ぐためにセラミックス等の耐摩耗材13が設けられており、同耐摩耗材13は、正方形状などに形成した多数のタイル片を接着材などで貼り付けることにより固着されている。
【0014】
次に、本発明の実施の形態に係る微粉炭濃度調整装置の作用につき説明する。
まず、石炭ミル4から微粉炭1が空気輸送により各微粉炭管5a〜5d内に送られると、同微粉炭1は、矢印A方向で示すように、1次分配器6a〜6dへ向かって微粉炭管5a〜5d内を流れる。そして、微粉炭1は、図3に示す如く、重力沈降によって微粉炭管5a〜5dの下部を流れるが、この際、固気二相流調整手段のキッカブロック12の傾斜面12aに当たって、上方へ巻き上げられことになり、最下層の高濃度部分が分散されながら1次分配器6a〜6dの入口に流れ込む。
しかる後、このような高濃度部分が分散された微粉炭1は、1次分配器6a〜6dの各段の流路10から矢印B,C方向で示すように分割されながら下流側の分岐管7,8内を流れ、火炉3に取付けた各バーナ2a〜2hへ供給され、同バーナ2a〜2hで燃焼されることになる。
【0015】
本発明の実施の形態に係る微粉炭濃度調整装置では、1次分配器6a〜6dの上流側に位置する微粉炭管5a〜5dの下部に傾斜面12aを備えたキッカブロック12が全巾に沿って設けられているため、微粉炭管5a〜5dの下部を流れる微粉炭1を上方へ分散させて混合させることができ、1次分配器6a〜6dの下流側に位置する左右の分岐管7,8及び各バーナ2a〜2hへ供給する微粉炭1の配分の均一化が図れる。このキッカブロック12による高さ方向の濃度分布改善効果確認試験を実施したところ、図4に示すような結果が得られた。同図から明らかなように、改善前に比べて改善後は、キッカブロック12の設置によって、微粉炭管5a〜5dの最下層の高濃度部分が分散され、各1次分配器6a〜6dの入口における上下方向の濃度分布のばらつきが減少し、均一化されていることが判る。
また、本実施の形態のキッカブロック12は、傾斜面12aの角度θが可変に構成されているため、装置完成後でも分岐管7,8及びバーナ2a〜2hへの分配割合を容易に変更でき、同バーナ2a〜2hの燃焼調整に役立ち、NOx・未燃分の低減に役立つ。しかも、キッカブロック12の傾斜面12aには、耐摩耗材13が設けられているため、同キッカブロック12の耐久性を向上させることができる。
【0016】
以上、本発明の実施形態につき述べたが、本発明は既述の実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲内において各種の変形及び変更を加え得るものである。例えば、本実施の形態では、1次分配器6a〜6dの下流側で2本の分岐管7,8に分配しているが、3本以上の分岐管に分配する1次分配器の上流側にキッカブロック12を設けることも可能である。
【0017】
【発明の効果】
上述の如く、本発明に係る微粉炭濃度調整装置は、微粉炭が気送されて流れる微粉炭管に接続されると共に、下流側の複数の分岐管に接続され、上下左右にわたって形成された複数段の流路より前記微粉炭を各分岐管に分配して気送する1次分配器を備え、該1次分配器の上流側で前記微粉炭管内の下部に、前記分岐管への微粉炭濃度を調整する固気二相流調整手段を設けたものであって、前記固気二相流調整手段は、前記微粉炭管の全巾に沿って設けられ、かつ上面が前記微粉炭の流れの方向に対して徐々に立ち上がる傾斜面を備えたキッカブロックであり、該キッカブロックは、前記微粉炭管内の下部を流れる微粉炭の濃度に応じて傾斜面の角度が調整可能に構成されているので、微粉炭管の下部を流れる微粉炭を上方へ分散させて混合させることが可能となり、かつ装置完成後でも分岐管への分配割合を容易に変更でき、1次分配器の入口における上下方向の濃度分布のばらつきを減少させて濃度分布の改善を図り、最終的に各バーナへの微粉炭配分を均一化でき、NOx・未燃分の低減に役立たせることができる
【図面の簡単な説明】
【図1】本発明の実施の形態に係る微粉炭濃度調整装置が適用される1次分配器の取付位置を示す概念図である。
【図2】本発明の実施の形態に係る微粉炭濃度調整装置及び1次分配器の設置付近を示す斜視図である。
【図3】本発明の実施の形態に係る微粉炭濃度調整装置を設けた微粉炭管内を流れる微粉炭の分散状態を示す概念図である。
【図4】本発明の実施の形態に係る微粉炭濃度調整装置によって改善された効果を確認する試験結果を示す線図である。
【図5】従来の1次分配器の設置付近を示す斜視図である。
【符号の説明】
1 微粉炭
2a〜2h 微粉炭バーナ
3 火炉
4 石炭ミル
5a〜5d 微粉炭管
6a〜6d 1次分配器
7,8 分岐管
9 仕切板
10 流路
11 盲板
12 キッカブロック(固気二相流調整手段)
12a 傾斜面
13 耐摩耗材
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a pulverized coal concentration adjusting device in a pulverized coal pipe for supplying pulverized coal to a burner attached to a furnace of a pulverized coal combustion boiler.
[0002]
[Prior art]
A plurality of pulverized coal burners are attached to the furnace of the pulverized coal combustion boiler, and one primary distributor is provided for each of the two burners. This primary distributor has a small space for use near the coal mill, prevents the complication of the piping of the pulverized coal pipe (duct), and reduces the material cost. It is provided so that the pulverized coal pipe of the book can be shared.
[0003]
An example of the primary distributor is shown in FIG. The primary distributor 51 is connected to a pulverized coal pipe 53 in which pulverized coal 52 is sent by air and flows in the direction of arrow A, and branch pipes 54 and 55 branched to the left and right sides at a downstream position. In the interior, a plurality of stages of flow paths partitioned by a plurality of partition plates 56 are formed vertically and horizontally. Blind plates 57 are alternately arranged on the left and right sides in the vertical direction at the downstream ends of the flow paths of these stages, and the blind plates 57 block communication with one of the branch pipes 54 and 55. The pulverized coal 52 is blown into the flows 54 and 55 in a flow divided in the left and right directions (arrow B direction and C direction).
[0004]
That is, the pulverized coal 52 pulverized by a coal mill (not shown) is pneumatically transported to the primary distributor 51 through a plurality of pulverized coal pipes 53 and branched from each flow path of the primary distributor 51. It is supplied to a plurality of burners (not shown) provided in the furnace through the tubes 54 and 55 and burned by the burners.
[0005]
[Problems to be solved by the invention]
However, since the pulverized coal 52 that is pneumatically transported in the pulverized coal pipe 53 has a larger mass than air and tends to gravity settle, the concentration of the pulverized coal 52 flowing under the pulverized coal pipe 53 is high. The concentration distribution in the vertical direction becomes uneven at the inlet of the secondary distributor 51, and the distribution of the pulverized coal 52 supplied from the respective flow paths of the primary distributor 51 to the respective burners via the left and right branch pipes 54 and 55 is different. May occur, leading to an increase in NOx / unburned content.
[0006]
The present invention has been made in view of such a situation, and its object is to improve the concentration distribution in the vertical direction at the inlet of the primary distributor and to make the distribution of pulverized coal to each burner uniform. An object of the present invention is to provide a pulverized coal concentration adjusting device capable of achieving the above.
[0007]
[Means for Solving the Problems]
In order to achieve the above-described problems of the prior art, the present invention is connected to a pulverized coal pipe in which pulverized coal is flown and flows, and is connected to a plurality of downstream branch pipes, and is formed over the top , bottom, left and right. A primary distributor that distributes and feeds the pulverized coal to each branch pipe from a plurality of stages of flow paths, and the pulverized powder to the branch pipe at a lower portion in the pulverized coal pipe on the upstream side of the primary distributor; A pulverized coal concentration adjusting device provided with solid-gas two-phase flow adjusting means for adjusting the charcoal concentration, wherein the solid-gas two-phase flow adjusting means is provided along the entire width of the pulverized coal pipe, and an upper surface thereof It is a kicker block having an inclined surface that gradually rises with respect to the flow direction of the pulverized coal, and the angle of the inclined surface can be adjusted according to the concentration of the pulverized coal flowing in the lower part of the pulverized coal pipe. It is configured .
[0008]
In the present invention, a wear-resistant material is provided on the inclined surface of the kicker block.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail based on illustrated embodiments. Here, FIG. 1 is a conceptual diagram of an attachment position of a primary distributor to which a pulverized coal concentration adjusting device according to an embodiment of the present invention is applied, and FIG. 2 is a pulverized coal concentration adjusting device and 1 according to the present embodiment. 3 is a perspective view of the vicinity of the installation of the next distributor, FIG. 3 is a conceptual diagram of a dispersion state of pulverized coal flowing through the pulverized coal pipe provided with the pulverized coal concentration adjusting device of FIG. 2, and FIG. 4 is a pulverized coal concentration adjustment of the present embodiment The diagram of the improvement effect confirmation test result by an apparatus is shown.
[0010]
The pulverized coal combustion boiler to which the pulverized coal concentration adjusting apparatus according to the embodiment of the present invention is applied generates heat by burning the supplied pulverized coal 1 with a pulverized coal burner 2, as shown in FIGS. A heat transfer tube group (not shown) that is arranged in parallel at a predetermined pitch above the furnace 3 to be generated, and that generates steam at a predetermined pressure and temperature by flowing steam inside and transmitting combustion heat from outside to generate heat. The combustion gas emitted from the pulverized coal combustion boiler is configured to be discharged from the chimney via an air preheater, an electric dust collector or the like (not shown).
Moreover, in connection with the said pulverized coal combustion boiler, the coal mill 4 which manufactures the pulverized coal 1 by grind | pulverizing the supplied coal is equipped, and the pulverized coal 1 is supplied from the coal mills 4 to 4 by pneumatic transportation. Eight pulverized coals that pass through the four pulverized coal pipes 5a to 5d, pass through the four primary distributors 6a to 6d and the branch pipes 7 and 8, and are attached to the outer periphery of the furnace 3 at a predetermined interval. It is supplied to each of the burners 2a to 2h.
[0011]
The primary distributors 6a to 6d have the same structure as in the prior art, and the pulverized coal 1 is fed by air and flows in the direction of arrow A, and the pulverized coal pipes 5a to 5d branch to the left and right sides at the downstream position. A plurality of flow paths 10 partitioned by a plurality of partition plates 9 are formed in the upper, lower, left, and right sides. On the downstream end side of the flow paths 10 of these stages, blind plates 11 are alternately arranged in the left and right directions in the vertical direction, and the blind plate 11 blocks communication with one of the branch pipes 7 and 8. In the branch pipes 7 and 8, the pulverized coal 1 is inflated by the flow divided into the left and right in the arrow B direction and the arrow C direction.
[0012]
Further, on the upstream side of the inlets of the primary distributors 6a to 6d, in the lower part of the pulverized coal pipes 5a to 5d, as shown in FIGS. A kicker block 12 of solid-gas two-phase flow adjusting means for adjusting the pulverized coal concentration to 7 and 8 is provided. The kicker block 12 constitutes the pulverized coal concentration adjusting device according to the embodiment of the present invention, and is provided along the entire width of the pulverized coal pipes 5a to 5d. An inclined surface 12a having an angle θ that gradually rises with respect to the flow direction (arrow A direction) is provided. That is, the kicker block 12 is formed on the downstream side (the inlet side of the primary distributors 6a to 6d) by the inclined surface 12a, and is formed in a substantially triangular cross section when viewed from the side. In addition, the code | symbol D has shown the pulverized coal density distribution in the pulverized coal pipes 5a-5d in FIG.
[0013]
In addition, the kicker block 12 can adjust the angle θ of the inclined surface 12a according to the concentration of the pulverized coal 1 flowing under the pulverized coal pipes 5a to 5d by using a known height position changing means or the like. It is configured. This adjustment operation of the angle θ is normally performed during the test operation after the completion of the apparatus, and each burner 2a to 2h during operation is changed and adjusted by changing the pulverized coal concentration to the branch pipes 7 and 8 on both the left and right sides. The distribution of the pulverized coal 1 is evenly distributed.
Further, the inclined surface 12a of the kicker block 12 is provided with a wear-resistant material 13 such as ceramics in order to prevent wear caused by the passing pulverized coal 1, and the wear-resistant material 13 includes a number of squares and the like. The tile pieces are fixed by attaching them with an adhesive or the like.
[0014]
Next, the operation of the pulverized coal concentration adjusting apparatus according to the embodiment of the present invention will be described.
First, when the pulverized coal 1 is sent from the coal mill 4 into the pulverized coal pipes 5a to 5d by pneumatic transportation, the pulverized coal 1 is directed to the primary distributors 6a to 6d as indicated by the arrow A direction. It flows in the pulverized coal pipes 5a to 5d. As shown in FIG. 3, the pulverized coal 1 flows under the pulverized coal pipes 5a to 5d by gravity sedimentation. At this time, the pulverized coal 1 hits the inclined surface 12a of the kicker block 12 of the solid-gas two-phase flow adjusting means and moves upward. As a result, the high concentration portion in the lowermost layer flows into the inlets of the primary distributors 6a to 6d while being dispersed.
Thereafter, the pulverized coal 1 in which such a high-concentration portion is dispersed is divided as shown by the arrows B and C from the flow passages 10 of the respective stages of the primary distributors 6a to 6d, while being branched downstream. 7, 8 is supplied to the burners 2a to 2h attached to the furnace 3, and burned by the burners 2a to 2h.
[0015]
In the pulverized coal concentration adjusting apparatus according to the embodiment of the present invention, the kicker block 12 provided with the inclined surface 12a at the lower part of the pulverized coal pipes 5a to 5d located on the upstream side of the primary distributors 6a to 6d is full-width. Therefore, the pulverized coal 1 flowing in the lower part of the pulverized coal pipes 5a to 5d can be dispersed and mixed upward, and the left and right branch pipes located on the downstream side of the primary distributors 6a to 6d. 7, 8 and the distribution of the pulverized coal 1 supplied to the burners 2a to 2h can be made uniform. When the density distribution improvement effect confirmation test in the height direction by the kicker block 12 was performed, the results as shown in FIG. 4 were obtained. As is clear from the figure, after the improvement as compared with before the improvement, the high concentration portion of the lowermost layer of the pulverized coal pipes 5a to 5d is dispersed by the installation of the kicker block 12, and the primary distributors 6a to 6d are dispersed. It can be seen that the variation in the concentration distribution in the vertical direction at the entrance is reduced and uniform.
In addition, since the kicker block 12 of the present embodiment is configured so that the angle θ of the inclined surface 12a is variable, the distribution ratio to the branch pipes 7 and 8 and the burners 2a to 2h can be easily changed even after the apparatus is completed. It is useful for adjusting the combustion of the burners 2a to 2h, and for reducing NOx / unburned content. In addition, since the wear resistant material 13 is provided on the inclined surface 12a of the kicker block 12, the durability of the kicker block 12 can be improved.
[0016]
As mentioned above, although embodiment of this invention was described, this invention is not limited to above-mentioned embodiment, In the range which does not deviate from the summary of this invention, a various deformation | transformation and change can be added. For example, in the present embodiment, the distribution is made to the two branch pipes 7 and 8 on the downstream side of the primary distributors 6a to 6d, but the upstream side of the primary distributor that distributes to three or more branch pipes. It is also possible to provide the kicker block 12.
[0017]
【The invention's effect】
As described above, the pulverized coal concentration adjusting device according to the present invention is connected to a pulverized coal pipe through which pulverized coal is flowed and is connected, and is connected to a plurality of downstream branch pipes, and is formed across the upper , lower, left and right sides. A primary distributor that distributes and feeds the pulverized coal to each branch pipe from a flow path in a stage, and pulverized coal to the branch pipe at a lower portion in the pulverized coal pipe on the upstream side of the primary distributor; Solid-gas two-phase flow adjusting means for adjusting the concentration is provided , the solid-gas two-phase flow adjusting means is provided along the entire width of the pulverized coal pipe, and the upper surface is a flow of the pulverized coal. The kicker block has an inclined surface that gradually rises with respect to the direction, and the kicker block is configured such that the angle of the inclined surface can be adjusted in accordance with the concentration of pulverized coal flowing in the lower part of the pulverized coal pipe . So pulverized coal flowing in the lower part of the pulverized coal pipe is dispersed and mixed upward Cause it becomes possible, and the distribution ratio of the device after completion even branch pipe can easily change, Ri FIG improved vertical is brought to a concentration distribution decreasing the variation in the concentration distribution of the inlet of the primary distributor, the final to be uniform pulverized coal distributed to each burner can Taseru useful standing in reducing NOx · unburned.
[Brief description of the drawings]
FIG. 1 is a conceptual diagram showing a mounting position of a primary distributor to which a pulverized coal concentration adjusting apparatus according to an embodiment of the present invention is applied.
FIG. 2 is a perspective view showing the vicinity of the installation of the pulverized coal concentration adjusting device and the primary distributor according to the embodiment of the present invention.
FIG. 3 is a conceptual diagram showing a dispersion state of pulverized coal flowing in a pulverized coal pipe provided with a pulverized coal concentration adjusting device according to an embodiment of the present invention.
FIG. 4 is a diagram showing test results for confirming the effect improved by the pulverized coal concentration adjusting apparatus according to the embodiment of the present invention.
FIG. 5 is a perspective view showing the vicinity of the installation of a conventional primary distributor.
[Explanation of symbols]
1 pulverized coal 2a to 2h pulverized coal burner 3 furnace 4 coal mills 5a to 5d pulverized coal pipes 6a to 6d primary distributors 7, 8 branch pipes 9 partition plates 10 flow paths 11 blind plates 12 kicker block (solid-gas two-phase flow Adjustment means)
12a Inclined surface 13 Wear resistant material

Claims (2)

微粉炭が気送されて流れる微粉炭管に接続されると共に、下流側の複数の分岐管に接続され、上下左右にわたって形成された複数段の流路より前記微粉炭を各分岐管に分配して気送する1次分配器を備え、該1次分配器の上流側で前記微粉炭管内の下部に、前記分岐管への微粉炭濃度を調整する固気二相流調整手段を設けた微粉炭濃度調整装置であって、前記固気二相流調整手段は、前記微粉炭管の全巾に沿って設けられ、かつ上面が前記微粉炭の流れの方向に対して徐々に立ち上がる傾斜面を備えたキッカブロックであり、該キッカブロックは、前記微粉炭管内の下部を流れる微粉炭の濃度に応じて傾斜面の角度が調整可能に構成されていることを特徴とする微粉炭濃度調整装置。The pulverized coal is connected to a plurality of pulverized coal pipes that are flown by air and connected to a plurality of downstream branch pipes, and the pulverized coal is distributed to the respective branch pipes through a plurality of stages of flow paths formed vertically and horizontally. comprising a primary distributor for pneumatically conveys Te, the lower portion of the pulverized coal pipe at the upstream side of the primary distributor, provided with a solid-gas two-phase flow adjusting means for adjusting the pulverized coal concentration to the branch pipe pulverized In the coal concentration adjusting device, the solid-gas two-phase flow adjusting means includes an inclined surface that is provided along the entire width of the pulverized coal pipe and whose upper surface gradually rises with respect to the flow direction of the pulverized coal. A pulverized coal concentration adjusting device, characterized in that the angle of the inclined surface can be adjusted according to the concentration of pulverized coal flowing in the lower part of the pulverized coal pipe . 前記キッカブロックの傾斜面には、耐摩耗材が設けられていることを特徴とする請求項1に記載の微粉炭濃度調整装置。The kicker on the inclined surface of the block, pulverized coal concentration adjustment apparatus according to claim 1, characterized that you have wear resistant material is provided.
JP25100899A 1999-09-06 1999-09-06 Pulverized coal concentration adjustment device Expired - Lifetime JP3746642B2 (en)

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US9797599B2 (en) * 2011-01-20 2017-10-24 Babcock Power Services, Inc. Coal flow balancing devices
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