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JPS6410732B2 - - Google Patents
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JPS6410732B2 - - Google Patents

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Publication number
JPS6410732B2
JPS6410732B2 JP4522384A JP4522384A JPS6410732B2 JP S6410732 B2 JPS6410732 B2 JP S6410732B2 JP 4522384 A JP4522384 A JP 4522384A JP 4522384 A JP4522384 A JP 4522384A JP S6410732 B2 JPS6410732 B2 JP S6410732B2
Authority
JP
Japan
Prior art keywords
pulverized coal
boiler
tube
pipe
distribution
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
JP4522384A
Other languages
Japanese (ja)
Other versions
JPS60188725A (en
Inventor
Yoshuki Iochi
Ryuichi Ueda
Susumu Akieda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ISOBE TETSUKO KK
Original Assignee
ISOBE TETSUKO KK
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 ISOBE TETSUKO KK filed Critical ISOBE TETSUKO KK
Priority to JP4522384A priority Critical patent/JPS60188725A/en
Publication of JPS60188725A publication Critical patent/JPS60188725A/en
Publication of JPS6410732B2 publication Critical patent/JPS6410732B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は微粉炭焚ボイラにおける、各微粉炭バ
ーナへの微粉炭供給量を均一に分配する、いわゆ
る微粉炭分配装置に関するものである。微粉炭を
ボイラの各微粉炭バーナへ均一に分配することの
重要性は下記にある。 (1) 窒素酸化物(NOX)排出量の低減 近来、NOX排出量を低減させることは国民
的課題であり、環境問題としては最大関心事の
ひとつである。微粉炭焚ボイラよりのNOX排
出量の増加は微粉炭分配の不均一に係る要素が
非常に多いため、本発明による微粉炭の均一分
配装置は微粉炭焚ボイラのNOX低減対策とし
て重要環境設備である。 (2) ボイラ効率の向上 微粉炭が不均一に分配された場合、ボイラの
各バーナの空燃比率が乱れ、空気過剰燃焼のバ
ーナと空気不足燃焼のバーナを生じ、ボイラ効
率が低下する。又空燃比率の乱れにより、未然
ダストの発生量が増加するため、このダストの
ボイラチユーブ付着量が増加し、この面からも
ボイラ効率の低下を招く。したがつて本発明の
微粉炭均一分配装置はボイラ効率の向上からも
重要設備である。 (3) ボイラチユーブおよびバーナ廻り部品の耐用
年数の向上 微粉炭が不均一に分配された場合、上記(2)の
如く空燃比率の乱れにより、微粉炭の燃焼温度
が各バーナにより高低を生じる。この結果、高
温部分のボイラチユーブ及びバーナ廻り部品の
耐用年数が低下する。この意味から微粉炭を均
一分配し、均一な燃焼温度を得ることは重要で
ある。 (4) ボイラ内耐火物の耐用年数の向上 上記(3)と同じ理由により、微粉炭の不均一分
配はボイラ内耐火物の耐用年数を著しく低下さ
せる。従つて微粉炭の均一分配装置は耐火物の
耐用年数の向上からも重要設備である。 以上の様に微粉炭をボイラの各バーナへ均一に
分配することは、環境面、省エネルギー面及び装
置保全の面から非常に重要なことであることがわ
かる。なおここでいう均一分配とは重量の均一分
配はもちろんのこと、粒度の均一分配という意味
も含む。 微粉炭は石炭粉砕機(ミル)により200メツシ
ユアンダーが80%以上になるまで粉砕され、空気
輸送によりボイラの各バーナへ送られて微粉炭燃
焼をする。微粉炭は石炭粉砕機(ミル)出口より
1基の分配器につき通常2〜4本のバーナへ分配
される。又ボイラ負荷の増減や、始動時又は停止
時に分配数の増減を行う場合がある。石炭粉砕機
(ミル)から各バーナ迄は微粉炭管内を通常30〜
40m/sの流速にて空気輸送されている。 従来の微粉炭の分配器・偏流管としては、特開
昭56−141232号公報に角型直角ベンド管に分配管
を接続した構造の粉粒体の分配装置が、又丸型の
直角ベンド管に分配管を接続した構造の分配装置
が特開昭58−110908号公報に開示されている。 前者の特開昭56−141232号公報の分配装置で
は、偏流が直角ベンド管の管の曲りの曲率による
だけであるため偏流が不充分である。又直角ベン
ド管の曲りの中間壁面の衝撃摩耗が大きい。更に
垂直輸送路にするためには水平の分配管以後を90
℃変曲させねばならず、それだけ圧力損失、ベン
ド部分の摩耗を発生させるという問題点がある。 次に後者は丸型ベンド管を使用しているので円
の上半と下半とに微粉炭の密度が変化し、微粉炭
の平均密度が同一となるように複数に分配するこ
とが難しい。更に、前者同様にベンド管の曲率だ
けでの偏流であるので偏流の程度が小さい。 本発明は従来のかかる問題点を解決し、簡単な
構造で強い偏流を生起して均一な分配を達成し、
しかも圧力損失、摩耗による寿命の低下も少ない
という優れた微粉炭焚ボイラのおける微粉炭の均
一分配装置を提供せんとするものである。 本発明の要旨は、微粉炭焚ボイラにおいて、ボ
イラのバーナへ微粉炭を空気輸送する垂直の微粉
炭輸送路途中に角型片寄りベント管状の偏流管を
設け、しかも同偏流管のもつ二つの曲りの最初の
曲りの曲率中心から遠い方の側壁の内周面の略変
曲点位置にデフレクターブロツクを設け、又偏流
管の出口側に偏流した微粉炭を複数の区画壁で均
一に複数分割する分配器を接続し、偏流管の二つ
の曲りとデフレクターブロツクによつて微粉炭空
気流に強い流れの屈曲を与えて輸送中の微粉炭を
慣性力と遠心力により偏流させて分配器で均一に
分配することを特徴とする微粉炭焚ボイラにおけ
る微粉炭の均一分配装置にある。 本発明では偏流管として片寄りベント管を使用
しているので入口・出口とも垂直流となつてお
り、短かいパスでもつて偏流を起こして垂直空気
輸送が続行される。 偏流は片寄りベント管の持つ二つの曲りとその
変曲点に設けたデフレクターブロツクによつて生
起される。デフレクターブロツクがあることで最
初の曲りの曲率半径は、片寄りベント管の外形状
のもつ曲率半径より小さくでき、より強い偏流を
最初の曲りで発生させている。又、これに続く第
2の曲りにおいてもこのデフレクターブロツクで
微粉炭の沿つて流れる内壁面が逆側の内壁面に移
る。その時の流れの屈曲はより短い曲率半径とな
るので、その偏流はきわめて強力なものとなる。 又衝撃摩耗を受けやすい第1の曲り変曲点部分
にはデフレクターブロツクを設けているので偏流
管の摩耗による損耗は少なく寿命を長いものにで
きる。更に、偏流管の管路は短かいので圧力損失
も低いものにできている。以下実施例を図面に基
いて説明する。 第1図に示す如く石炭粉砕機(ミル)1出口の
微粉炭管2内の微粉炭と空気の固気2相流は回転
流等の非整流となつているため、整流器3により
整流し直線流する。又微粉炭管2は通常円形であ
るため、円角管4を設けて角管とする。この後に
30゜〜90゜の適当な角度を有した偏流管5を設けて
上記固気2相流を偏流させる。固気2相流中の微
粉炭はその真比重が2.0〜2.3と空気より重いた
め、慣性力(inertia)及び遠心力により偏流管
5の外面に偏つた流になる。これは偏流管5内周
壁に三角状に突出したデフレクターブロツク10
により偏流が強制されより確実となるものであ
る。微粉炭が均一偏流となつたところで分配器6
にて分配する。微粉炭と空気の流れを第4図に示
している。分配数は通常2〜4であるが第2図は
3分配の場合の分配器を示す。第3図は分配器の
−線における断面図を示す。カツトダンパ
7,8,9は通常開とするが、ボイラの負荷変動
等により、上記カツトダンパの内1個又は2個を
閉とする場合があるがこの場合でも分配効率は良
好でなければならない。 次に3分配の場合の本発明による微粉炭分配装
置の分配効率のテストデータを示す。 (1) 3分配の分配効率(カツトダンパ7,8,9
全開)
The present invention relates to a so-called pulverized coal distribution device that uniformly distributes the amount of pulverized coal supplied to each pulverized coal burner in a pulverized coal-fired boiler. The importance of uniformly distributing pulverized coal to each pulverized coal burner of the boiler is explained below. (1) Reducing nitrogen oxide (NOX) emissions In recent years, reducing NOX emissions has become a national issue and one of the greatest environmental concerns. The increase in NOX emissions from pulverized coal-fired boilers is due to many factors related to uneven distribution of pulverized coal, so the pulverized coal uniform distribution device of the present invention is an important environmental facility as a measure to reduce NOx in pulverized coal-fired boilers. be. (2) Improving boiler efficiency If pulverized coal is distributed unevenly, the air-fuel ratio of each burner in the boiler will be disturbed, causing some burners to burn with excess air and others to burn with insufficient air, reducing boiler efficiency. Furthermore, the amount of dust generated increases due to the disturbance in the air-fuel ratio, which increases the amount of dust that adheres to the boiler tube, which also causes a decrease in boiler efficiency. Therefore, the pulverized coal uniform distribution device of the present invention is important equipment from the standpoint of improving boiler efficiency. (3) Improving the service life of the boiler tube and parts around the burner If pulverized coal is distributed unevenly, the combustion temperature of pulverized coal will vary depending on each burner due to the disturbance in the air-fuel ratio as described in (2) above. . As a result, the service life of the boiler tube and parts surrounding the burner, which are high-temperature parts, is reduced. From this point of view, it is important to uniformly distribute pulverized coal and obtain a uniform combustion temperature. (4) Improving the service life of the refractories in the boiler For the same reason as (3) above, uneven distribution of pulverized coal significantly reduces the service life of the refractories in the boiler. Therefore, a device for uniformly distributing pulverized coal is an important piece of equipment for improving the service life of refractories. As described above, it can be seen that uniformly distributing pulverized coal to each burner of a boiler is extremely important from the viewpoints of environment, energy saving, and equipment maintenance. Note that uniform distribution here includes not only uniform distribution of weight but also uniform distribution of particle size. The pulverized coal is pulverized by a coal pulverizer (mill) until the 200-mesh under is 80% or more, and then sent by air to each burner of the boiler for pulverized coal combustion. Pulverized coal is distributed from the outlet of a coal crusher (mill) to usually two to four burners per distributor. In addition, the boiler load may be increased or decreased, or the distribution number may be increased or decreased at the time of starting or stopping. From the coal crusher (mill) to each burner, the inside of the pulverized coal pipe is usually 30~
It is pneumatically transported at a flow rate of 40 m/s. As conventional pulverized coal distributors and drift pipes, Japanese Patent Application Laid-Open No. 141232/1983 discloses a powder distribution device having a structure in which a distribution pipe is connected to a square right-angled bent pipe, and a round right-angled bent pipe. A distribution device having a structure in which a distribution pipe is connected to a distribution pipe is disclosed in Japanese Patent Application Laid-Open No. 110908/1983. In the former distribution device disclosed in Japanese Patent Application Laid-Open No. 56-141232, the deflection is caused only by the curvature of the right-angle bent pipe, and therefore the deflection is insufficient. In addition, impact wear on the intermediate wall surface of the right-angle bend pipe is large. Furthermore, in order to make it a vertical transportation route, the area after the horizontal distribution pipe is 90
There is a problem in that the bending has to be performed by degrees Celsius, which increases pressure loss and wear at the bend portion. Secondly, since the latter uses a round bent pipe, the density of the pulverized coal changes between the upper and lower halves of the circle, making it difficult to distribute the pulverized coal into multiple pieces so that the average density is the same. Furthermore, like the former, the degree of drift is small because the drift is caused only by the curvature of the bent pipe. The present invention solves these conventional problems and achieves uniform distribution by generating strong drift with a simple structure.
Moreover, it is an object of the present invention to provide a device for uniformly distributing pulverized coal in a pulverized coal-fired boiler, which is excellent in that there is little reduction in life due to pressure loss and wear. The gist of the present invention is that, in a pulverized coal-fired boiler, a rectangular bent pipe-like deflection pipe is provided in the middle of a vertical pulverized coal transport path for pneumatically transporting pulverized coal to the burner of the boiler, and two A deflector block is provided at approximately the inflection point position of the inner circumferential surface of the side wall farthest from the center of curvature of the first bend, and the pulverized coal that has drifted toward the outlet side of the drift tube is evenly divided into multiple sections by multiple partition walls. The two bends in the deflector tube and the deflector block give the pulverized coal airflow a strong flow bend, and the pulverized coal being transported is deflected by inertial force and centrifugal force, and is uniformly distributed by the distributor. The present invention provides a device for uniformly distributing pulverized coal in a pulverized coal-fired boiler. In the present invention, since a biased bent pipe is used as a biased flow pipe, the flow is vertical at both the inlet and the outlet, and vertical air transport is continued by causing a drift even in a short path. The drifted flow is caused by the two bends of the lopsided vent pipe and the deflector blocks installed at the points of inflection. Due to the presence of the deflector block, the radius of curvature of the first bend can be made smaller than the radius of curvature of the outer shape of the offset vent pipe, thereby generating a stronger drifted flow at the first bend. Also, in the second bend following this, the inner wall surface along which the pulverized coal flows is shifted to the opposite inner wall surface by this deflector block. At that time, the bend in the flow has a shorter radius of curvature, so the drift becomes extremely strong. Furthermore, since a deflector block is provided at the first bending inflection point that is susceptible to impact wear, wear and tear of the deflection tube due to abrasion is reduced and the service life can be extended. Furthermore, since the channel of the deflection tube is short, the pressure loss is also low. Examples will be described below based on the drawings. As shown in Fig. 1, the solid two-phase flow of pulverized coal and air in the pulverized coal pipe 2 at the outlet of the coal crusher (mill) 1 is a non-rectified flow such as a rotating flow, so it is rectified by the rectifier 3 and straightened. Flow. Further, since the pulverized coal pipe 2 is usually circular, a circular square pipe 4 is provided to make it a square pipe. after this
A deflection pipe 5 having an appropriate angle of 30° to 90° is provided to deflect the solid-gas two-phase flow. Since the pulverized coal in the solid gas two-phase flow has a true specific gravity of 2.0 to 2.3, which is heavier than air, the flow is biased toward the outer surface of the deflection tube 5 due to inertia and centrifugal force. This is a deflector block 10 that protrudes triangularly from the inner peripheral wall of the deflection tube 5.
This forces the drifting flow and makes it more reliable. When the pulverized coal becomes uniformly distributed, the distributor 6
will be distributed at Figure 4 shows the flow of pulverized coal and air. The number of distributions is usually 2 to 4, but FIG. 2 shows a distributor for three distributions. FIG. 3 shows a cross-sectional view of the distributor along the - line. The cut dampers 7, 8, and 9 are normally open, but one or two of the cut dampers may be closed due to boiler load fluctuations, etc. Even in this case, the distribution efficiency must be good. Next, test data on the distribution efficiency of the pulverized coal distribution device according to the present invention in the case of three distributions will be shown. (1) Distribution efficiency of 3 distribution (cut damper 7, 8, 9
full throttle)

【表】 (2) 2分配の分配効率(カツトダンパ7閉、、カ
ツトダンパ8,9全開)
[Table] (2) Distribution efficiency of two distributions (cut damper 7 closed, cut dampers 8 and 9 fully open)

【表】 ※ 分配効率とは完全に等分配された場
合を100%とする。
又本発明による微粉炭分配装置の圧力損失のテ
ストデータを下表に示す。 (3) 3分配の圧力損失(カツトダンパ7,8,9
全開)
[Table] *Distribution efficiency is defined as 100% when distribution is completely equal.
Test data on pressure loss of the pulverized coal distribution device according to the present invention is shown in the table below. (3) Three distribution pressure loss (cut damper 7, 8, 9
full throttle)

【表】 (4) 2分配の圧力損失(カツトダンパ7閉、、カ
ツトダンパ8,9全開)
[Table] (4) Pressure loss in two distributions (cut damper 7 closed, cut dampers 8 and 9 fully open)

【表】 以上の様に本発明による微粉炭の均一分配装置
は従来の分配装置と比較すると下記の優れた効果
がある。 (1) 例えば従来のベンチユリータイプの分配装置
は微粉炭管直径の10倍以上の垂直々管部を必要
とするが本発明による偏流管タイプの分配装置
は直管部を、必要としないため、設備上非常に
有利である。 (2) 本発明による分配装置は構造が簡単であるた
め従来タイプに比較して圧力損失が1/2〜1/3と
少ない。従つて微粉炭輸送用空気の圧力が少な
くてよいため、大きな送風設備を必要としな
い。 (3) 分配効率については従来タイプが40〜80%で
あるのに比較して本発明による分配装置の分配
効率は常に90%以上の効率を維持できる。 (4) 偏流管として角型片寄りベンド管状のものを
使用し、しかもその変曲点位置にデフレクター
ブロツクを設けたことによつて、流れの屈曲の
曲率半径を小さくして2回の強い偏流を生起し
て偏流を充分なものとして均一な分配を可能と
した。又衝撃摩耗の激しい変曲点の位置にはデ
フレクターブロツクを設けているので偏流管の
寿命を長くできる。更に、短かいパスのうちに
偏流させることができ、圧力損失を少なくして
垂直輸送を続行できるという利点がある。
[Table] As described above, the pulverized coal uniform distribution device according to the present invention has the following excellent effects when compared with the conventional distribution device. (1) For example, a conventional ventilate type distribution device requires a vertical pipe section that is 10 times or more the diameter of the pulverized coal pipe, but the biased flow tube type distribution device according to the present invention does not require a straight pipe section. , which is very advantageous in terms of equipment. (2) Since the distribution device according to the present invention has a simple structure, the pressure loss is 1/2 to 1/3 lower than that of conventional types. Therefore, since the pressure of the air for transporting pulverized coal is low, large air blowing equipment is not required. (3) Regarding the distribution efficiency, compared to the conventional type which is 40 to 80%, the distribution efficiency of the distribution device according to the present invention can always maintain an efficiency of 90% or more. (4) By using a rectangular, one-sided bent tube as the deflection tube and installing a deflector block at the point of inflection, the radius of curvature of the bend in the flow is reduced, resulting in two strong deflections. This caused sufficient drift and enabled uniform distribution. Furthermore, since deflector blocks are provided at inflection points where impact wear is severe, the life of the deflection tube can be extended. Furthermore, there is an advantage that the flow can be deflected within a short path, and vertical transport can be continued with less pressure loss.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の微粉炭焚ボイラにおける微粉
炭の均一分配装置の実施例を示す正面図、第2図
は同実施例の分配器の構造を示す説明図、第3図
は第2図の−線における断面図、第4図は本
実施例での微粉炭と空気の流れを示す説明図であ
る。 1:石炭粉砕機(ミル)、2:微粉炭管、3:
整流器、4:円角管、5:偏流管、6:分配器、
7,8,9:カツトダンパ、10:デフレクター
ブロツク。
FIG. 1 is a front view showing an embodiment of a pulverized coal uniform distribution device in a pulverized coal-fired boiler of the present invention, FIG. 2 is an explanatory diagram showing the structure of a distributor of the same embodiment, and FIG. FIG. 4 is an explanatory diagram showing the flow of pulverized coal and air in this embodiment. 1: Coal crusher (mill), 2: Pulverized coal pipe, 3:
Rectifier, 4: Circular tube, 5: Variation tube, 6: Distributor,
7, 8, 9: Cut damper, 10: Deflector block.

Claims (1)

【特許請求の範囲】[Claims] 1 微粉炭焚ボイラにおいて、ボイラのバーナへ
微粉炭を空気輸送する垂直の微粉炭輸送路途中に
角型片寄りベント管状の偏流管を設け、しかも同
偏流管のもつ二つの曲りの最初の曲りの曲率中心
から遠い方の側壁の内周面の略変曲点位置にデフ
レクターブロツクを設け、又偏流管の出口側に偏
流した微粉炭を複数の区画壁で均一に複数分割す
る分配器を接続し、偏流管の二つの曲りとデフレ
クターブロツクによつて微粉炭空気流に強い流れ
の屈曲を与えて輸送中の微粉炭を慣性力と遠心力
により偏流させて分配器で均一に分配することを
特徴とする微粉炭焚ボイラにおける微粉炭の均一
分配装置。
1. In a pulverized coal-fired boiler, a rectangular bent tube-shaped drift pipe is installed in the middle of the vertical pulverized coal transport path that pneumatically transports pulverized coal to the boiler's burner, and the first of the two bends of the drift pipe is A deflector block is provided at approximately the inflection point position of the inner circumferential surface of the side wall farthest from the center of curvature, and a distributor is connected to the outlet side of the deflection tube to evenly divide the deflected pulverized coal into a plurality of partition walls. The two bends of the deflector tube and the deflector block give strong flow bends to the pulverized coal airflow, and the pulverized coal being transported is deflected by inertial force and centrifugal force, and is evenly distributed by the distributor. Uniform distribution device for pulverized coal in a pulverized coal-fired boiler.
JP4522384A 1984-03-08 1984-03-08 Uniformly distributing device for pulverized coal in pulverized coal burning boiler Granted JPS60188725A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4522384A JPS60188725A (en) 1984-03-08 1984-03-08 Uniformly distributing device for pulverized coal in pulverized coal burning boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4522384A JPS60188725A (en) 1984-03-08 1984-03-08 Uniformly distributing device for pulverized coal in pulverized coal burning boiler

Publications (2)

Publication Number Publication Date
JPS60188725A JPS60188725A (en) 1985-09-26
JPS6410732B2 true JPS6410732B2 (en) 1989-02-22

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP4522384A Granted JPS60188725A (en) 1984-03-08 1984-03-08 Uniformly distributing device for pulverized coal in pulverized coal burning boiler

Country Status (1)

Country Link
JP (1) JPS60188725A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0484233U (en) * 1990-11-28 1992-07-22
US8082860B2 (en) 2008-04-30 2011-12-27 Babcock Power Services Inc. Anti-roping device for pulverized coal burners
US8104412B2 (en) * 2008-08-21 2012-01-31 Riley Power Inc. Deflector device for coal piping systems
CN105444197B (en) * 2014-08-27 2017-11-17 沈阳工程学院 A kind of second order one enters five and goes out divider system
CN105135462B (en) * 2015-08-21 2019-02-01 淮北市生产力促进中心 Coal even separator

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6023047B2 (en) * 1980-04-05 1985-06-05 川崎重工業株式会社 Method and device for distributing powder and granules in a gas stream
US4611543A (en) * 1981-12-17 1986-09-16 Combustion Engineering, Inc. Restrictor application for in line gas entrained solids redistribution

Also Published As

Publication number Publication date
JPS60188725A (en) 1985-09-26

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