JP2000046315A - Pulverized coal distributing device - Google Patents

Pulverized coal distributing device

Info

Publication number
JP2000046315A
JP2000046315A JP10211224A JP21122498A JP2000046315A JP 2000046315 A JP2000046315 A JP 2000046315A JP 10211224 A JP10211224 A JP 10211224A JP 21122498 A JP21122498 A JP 21122498A JP 2000046315 A JP2000046315 A JP 2000046315A
Authority
JP
Japan
Prior art keywords
pulverized coal
fine powder
distributor
pulverized
mixer
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.)
Pending
Application number
JP10211224A
Other languages
Japanese (ja)
Inventor
Mutsuo Kato
睦男 加藤
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP10211224A priority Critical patent/JP2000046315A/en
Publication of JP2000046315A publication Critical patent/JP2000046315A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To reduce the facility cost of a pulverized coal distributing device and to shorten the construction period of the device by making pulverized coal to be surely distributed without using any damper and, at the same time, omitting the troublesome adjusting work incidental to the damper by making the dispersed state of pulverized coal in a particle flow uniform before the flowing body reaches a pulverized coal mixer. SOLUTION: A pulverized coal distributing device is provided with a pulverized coal distributor 31 which branches a pulverized coal flow which is carried by a gas into a plurality of flows and a pulverized coal mixer 32 positioned on the upstream side of the distributor 31 and the mixer 32 is provided with a plurality of stages of elements 36 (a, b, and c) which are arranged perpendicularly to the axis. The elements 36 are constituted by arranging a required number of pulverized coal dispersing bars 37 (a, b, and c) in parallel with each other in the same plane. Consequently, pulverized coal can be distributed evenly by making the dispersed state of the pulverized coal in a particle flow uniform before the flow reaches the distributor 32.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は微粉炭を燃料とする
微粉炭焚ボイラ等、微粉炭を燃料とする設備の微粉炭供
給ラインに設けられる微粉炭分配装置に関するものであ
る。
The present invention relates to a pulverized coal distribution device provided in a pulverized coal supply line of a facility using pulverized coal as a fuel, such as a pulverized coal-fired boiler using pulverized coal as a fuel.

【0002】[0002]

【従来の技術】一般にボイラは負荷状態に応じて火力が
調整される様になっており、微粉炭焚ボイラに於いても
火力の調整が可能な様に複数のバーナを有し、負荷状態
に応じ、燃焼に供せられるバーナの燃焼を制限してい
る。前記微粉炭分配装置は微粉炭供給ラインで送給され
る微粉炭を前記複数のバーナに均等に分配する機能を課
せられている。
2. Description of the Related Art In general, a boiler has a heating power adjusted according to a load condition, and a pulverized coal-fired boiler has a plurality of burners so that the heating power can be adjusted. Accordingly, the combustion of the burner provided for combustion is restricted. The pulverized coal distribution device is provided with a function of evenly distributing the pulverized coal fed in the pulverized coal supply line to the plurality of burners.

【0003】先ず、微粉炭分配装置が設けられている微
粉炭焚ボイラ設備について、図3により略述する。
[0003] First, a pulverized coal-fired boiler provided with a pulverized coal distribution device will be briefly described with reference to FIG.

【0004】微粉炭焚ボイラ1には一次供給ライン2、
二次供給ライン3及び排気ライン4が接続され、該排気
ライン4の下流端は煙突15に接続されている。
The pulverized coal-fired boiler 1 has a primary supply line 2,
The secondary supply line 3 and the exhaust line 4 are connected, and the downstream end of the exhaust line 4 is connected to a chimney 15.

【0005】前記一次供給ライン2は上流側より配設さ
れた一次空気ファン5、一次空気予熱器6、微粉炭ミル
7、微粉炭分配装置8及び前記一次空気ファン5、一次
空気予熱器6の受熱部6a、微粉炭ミル7、微粉炭分配
装置8を順次接続する一次空気ダクト9、及び前記微粉
炭分配装置8と図示しないバーナとを接続する分岐ダク
ト10a,10b,10cから主に構成される。
The primary supply line 2 includes a primary air fan 5, a primary air preheater 6, a pulverized coal mill 7, a pulverized coal distribution device 8, and a primary air fan 5 and a primary air preheater 6 arranged from the upstream side. It mainly comprises a heat receiving section 6a, a pulverized coal mill 7, a primary air duct 9 for sequentially connecting the pulverized coal distribution device 8, and branch ducts 10a, 10b, 10c for connecting the pulverized coal distribution device 8 to a burner (not shown). You.

【0006】前記二次供給ライン3は上流側より配設さ
れた二次空気ファン11、二次空気予熱器12及び前記
二次空気ファン11、前記二次空気予熱器12の受熱部
12a、前記微粉炭焚ボイラ1を順次接続する二次空気
ダクト13により主に構成される。
The secondary supply line 3 includes a secondary air fan 11, a secondary air preheater 12, a secondary air fan 11, a heat receiving portion 12a of the secondary air preheater 12, It is mainly constituted by a secondary air duct 13 that sequentially connects the pulverized coal-fired boilers 1.

【0007】前記排気ライン4は上流側(微粉炭焚ボイ
ラ1側)より配設された一次空気予熱器6、排気ファン
14及び前記微粉炭焚ボイラ1、一次空気予熱器6の給
熱部6b、排気ファン14、煙突15を接続する排気ダ
クト16及び前記一次空気予熱器6をバイパスし途中に
前記二次空気予熱器12の給熱部12bが接続されたバ
イパスダクト17から主に構成される。
The exhaust line 4 includes a primary air preheater 6 and an exhaust fan 14 provided from an upstream side (pulverized coal-fired boiler 1 side), and a heat supply section 6b of the pulverized coal-fired boiler 1 and the primary air preheater 6. , An exhaust fan 16, an exhaust duct 16 that connects the chimney 15, and a bypass duct 17 that bypasses the primary air preheater 6 and is connected to the heat supply section 12 b of the secondary air preheater 12 on the way. .

【0008】一次空気は前記一次空気ファン5により前
記一次空気ダクト9を介して前記一次空気予熱器6の受
熱部6aを通過し、前記一次空気予熱器6の給熱部6b
を通過する排気ガスとの間で熱交換が行われ予熱され
る。予熱された一次空気は前記一次空気ダクト9を介し
て前記微粉炭ミル7へ導入される。該微粉炭ミル7は石
炭を流体搬送可能な微粉に粉砕するものであり、粉砕さ
れた微粉炭は前記一次空気と共に前記一次空気ダクト9
を介して前記微粉炭分配装置8に流入し、該微粉炭分配
装置8により分配され、前記各分岐ダクト10a,10
b,10cを介して前記各バーナ(図示せず)に供給さ
れる。
The primary air passes through the heat receiving section 6a of the primary air preheater 6 through the primary air duct 9 by the primary air fan 5 and the heat supply section 6b of the primary air preheater 6
Heat is exchanged with the exhaust gas passing through the preheater to be preheated. The preheated primary air is introduced into the pulverized coal mill 7 through the primary air duct 9. The pulverized coal mill 7 is for pulverizing coal into fine powder capable of carrying fluid, and the pulverized pulverized coal is mixed with the primary air in the primary air duct 9.
Flows into the pulverized coal distribution device 8 via the pulverized coal distribution device 8, and is distributed by the pulverized coal distribution device 8;
The burners (not shown) are supplied through b and 10c.

【0009】又、二次空気は前記二次空気ファン11に
より前記二次空気ダクト13を介して前記二次空気予熱
器12の受熱部12aを通過し、前記二次空気予熱器1
2の給熱部12bを通過する排気ガスとの間で熱交換が
行われ予熱される。予熱された二次空気は前記二次空気
ダクト13を介して前記微粉炭焚ボイラ1内に導入され
る。該微粉炭焚ボイラ1は前記一次空気供給ライン2よ
り供給された微粉炭を燃焼させ、蒸気を発生させる。燃
焼により生成された排気ガスは前記排気ファン14によ
り吸引され、前記微粉炭焚ボイラ1から前記排気ダクト
16に排出された後分流し、分流の一方は該排気ダクト
16を介して前記一次空気予熱器6の給熱部6bを通過
する。前記一次空気予熱器6の給熱部6bを通過する過
程で前記排気ガスは前記一次空気に給熱して所要の温度
迄冷却される。又、分流の他方は前記バイパスダクト1
7を介して前記二次空気予熱器12の給熱部12bを通
過し、通過過程で前記二次空気に給熱し、所要の温度に
冷却される。冷却された排気ガスは再び合流し、前記排
気ダクト16、前記煙突15を介して外部へ排出され
る。
The secondary air passes through the heat receiving portion 12a of the secondary air preheater 12 through the secondary air duct 13 by the secondary air fan 11, and the secondary air preheater 1
Heat exchange is performed between the exhaust gas passing through the second heat supply unit 12b and preheating. The preheated secondary air is introduced into the pulverized coal-fired boiler 1 through the secondary air duct 13. The pulverized coal-fired boiler 1 burns pulverized coal supplied from the primary air supply line 2 to generate steam. Exhaust gas generated by the combustion is sucked by the exhaust fan 14 and discharged from the pulverized coal-fired boiler 1 to the exhaust duct 16 and then split, and one of the split flows is preheated through the exhaust duct 16. It passes through the heat supply section 6b of the vessel 6. In the process of passing through the heat supply section 6b of the primary air preheater 6, the exhaust gas supplies heat to the primary air and is cooled to a required temperature. The other side of the branch is the bypass duct 1
The secondary air passes through the heat supply section 12b of the secondary air preheater 12 via the heater 7 and is supplied with heat to the secondary air during the passage, and is cooled to a required temperature. The cooled exhaust gas merges again and is discharged outside through the exhaust duct 16 and the chimney 15.

【0010】次に、従来の微粉炭分配装置8について図
4により説明する。
Next, a conventional pulverized coal distribution device 8 will be described with reference to FIG.

【0011】前記一次空気ダクト9に連続し、中空の胴
部21の下流端には漏斗状の分岐胴22a,22b,2
2cが連設され、該分岐胴22a,22b,22cの下
流端はそれぞれストップバルブ23a,23b,23c
を介して前記分岐ダクト10a,10b,10cに接続
されている。
[0011] A funnel-shaped branch body 22a, 22b, 2 is connected to the primary air duct 9 at the downstream end of the hollow body 21.
2c are continuously provided, and downstream ends of the branch cylinders 22a, 22b, 22c are respectively provided with stop valves 23a, 23b, 23c.
Are connected to the branch ducts 10a, 10b, and 10c through the connection.

【0012】微粉炭分配装置8に流入する気体搬送の微
粉炭の粉流体は、遠心力等により流体中の微粉炭が偏流
している。例えば、図4に示す様に、一次空気ダクト9
がL字状に曲がって前記胴部21に連設されているとす
ると、粉流体中の微粉炭は曲部25の外周側に偏在し、
粉流体中の微粉炭の分散状態は均一でなくなる。この
為、前記分岐胴22a,22b,22cで分配される微
粉炭量を均等とする為、前記分岐胴22aと分岐胴22
bとの境界部、分岐胴22bと分岐胴22cとの境界部
にダンパ24a,24bを回転可能に設け、該ダンパ2
4a,24bの傾斜を変え前記分岐胴22a,22b,
22cへの分岐口の面積を調整している。
In the pulverized coal powder fluid flowing into the pulverized coal distribution device 8, the pulverized coal in the fluid is drifted due to centrifugal force or the like. For example, as shown in FIG.
Is bent in an L-shape and connected to the body 21, the pulverized coal in the pulverized fluid is unevenly distributed on the outer peripheral side of the curved portion 25,
The dispersion state of the pulverized coal in the pulverized fluid is not uniform. Therefore, in order to equalize the amount of pulverized coal distributed in the branch cylinders 22a, 22b, 22c, the branch cylinder 22a and the branch cylinder 22
b, and at the boundary between the branch body 22b and the branch body 22c, the dampers 24a and 24b are rotatably provided.
4a, 24b, the branch cylinders 22a, 22b,
The area of the branch to 22c is adjusted.

【0013】前記ダンパ24a,24bの位置設定をす
る場合、実際に粉流体を繰返し流してみて、分配した粉
流体中の微粉炭が均等になる様な位置を探している。位
置を決定した後は前記ダンパ24a,24bは固定して
いる。
When the positions of the dampers 24a and 24b are set, the pulverized fluid is actually repeatedly flown to find a position where the pulverized coal in the distributed pulverized fluid becomes uniform. After the position is determined, the dampers 24a and 24b are fixed.

【0014】[0014]

【発明が解決しようとする課題】上述した様に、微粉炭
を均等に分配するには前記ダンパ24a,24bの調整
が必要であり、その調整作業は微粉炭分配装置単体では
調整が行えず、実際に粉流体を流して微粉炭の分散状態
を調べるという面倒なものであり、多くの時間を要して
いた。又、一度設定すると前記ダンパ24a,24bは
固定するので、稼働状況の変更があった場合、粉流体の
流れ状態に変化があった場合等に早急に対応ができない
という問題があった。
As described above, in order to distribute pulverized coal evenly, it is necessary to adjust the dampers 24a and 24b, and the adjustment operation cannot be performed by the pulverized coal distribution device alone. It is troublesome to check the dispersion state of the pulverized coal by actually flowing the pulverized fluid, and it took a lot of time. Further, once set, the dampers 24a and 24b are fixed, so that there is a problem that it is not possible to quickly respond to a change in the operating state or a change in the flow state of the powder fluid.

【0015】本発明は斯かる実情に鑑み、粉流体中の微
粉炭の分散状態を分岐胴に至る以前に均一化し、前記ダ
ンパを不要とし、均等な微粉炭の分配が確実に行えると
共に、該ダンパに付随する面倒な調整作業を省略し、設
備コストの低減、工期の短縮を図るものである。
In view of such circumstances, the present invention makes the dispersion state of the pulverized coal in the pulverized fluid uniform before reaching the branch cylinder, eliminates the need for the damper, and ensures the uniform distribution of the pulverized coal. The purpose of the present invention is to omit troublesome adjustment work associated with the damper, thereby reducing equipment costs and shortening the construction period.

【0016】[0016]

【課題を解決するための手段】本発明は、気体搬送の微
粉炭粉流を複数の流れに分岐する微粉炭分配器と該微粉
炭分配器の上流側に配設された微粉炭混合器とを具備
し、該微粉炭混合器が軸心と直交するエレメントを複数
段有し、該エレメントは所要数の微粉分散棒を同一面内
に平行に配設して成る微粉炭分配装置に係り、又、前記
微粉分散棒の上側、下側の隣接する段のエレメントは微
粉分散棒が前記微粉分散棒に対して直交する様に配置さ
れた微粉炭分配装置に係り、更に、前記微粉分散棒に対
し隔段のエレメントは該隔段の微粉分散棒が前記微粉分
散棒に対して平行で且つ前記微粉分散棒と微粉分散棒と
の中間に位置する微粉炭分配装置に係り、粉流体中の微
粉体の分散状態を微粉炭分配器に至る以前に均一化し、
微粉炭を均等に分配する。
SUMMARY OF THE INVENTION The present invention relates to a pulverized coal distributor for branching a pulverized coal powder stream for gas transport into a plurality of streams, and a pulverized coal mixer disposed upstream of the pulverized coal distributor. The pulverized coal mixer has a plurality of elements orthogonal to the axis, the element is related to a pulverized coal distribution device comprising a required number of fine powder dispersion rods arranged in parallel in the same plane, Further, the upper and lower adjacent elements of the fine powder dispersing rod relate to a pulverized coal distribution device in which the fine powder dispersing rod is arranged so as to be orthogonal to the fine powder dispersing rod. On the other hand, the element of the separated stage relates to a pulverized coal distribution device in which the fine powder dispersing rod of the separated stage is parallel to the fine powder dispersing rod and located between the fine powder dispersing rod and the fine powder dispersing rod. Homogenizing the dispersion state of the body before reaching the pulverized coal distributor,
Distribute pulverized coal evenly.

【0017】[0017]

【発明の実施の形態】以下、図面を参照しつつ本発明の
実施の形態を説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0018】図1中、図4中で示したものと同様のもの
には同符号を付してある。
In FIG. 1, the same components as those shown in FIG. 4 are denoted by the same reference numerals.

【0019】本微粉炭分配装置30は微粉炭分配器31
と該微粉炭分配器31の上流端に連設される微粉炭混合
器32から構成される。
The pulverized coal distributor 30 includes a pulverized coal distributor 31.
And a pulverized coal mixer 32 connected to the upstream end of the pulverized coal distributor 31.

【0020】前記微粉炭分配器31は前述した従来の微
粉炭分配装置8からダンパ24a,24bを取除いたも
のと同等であり、中空の胴部34の下流端には漏斗状の
分岐胴33a,33b,33cが連設され、該分岐胴3
3a,33b,33cの下流端はそれぞれストップバル
ブ23a,23b,23cを介して前記分岐ダクト10
a,10b,10cに接続されている。前記分岐胴33
a,33b,33cの開口面積比はバーナ(図示せず)
に送給する微粉炭量に応じて所定の値に設定されてい
る。
The pulverized coal distributor 31 is equivalent to the above-described conventional pulverized coal distribution device 8 in which the dampers 24a and 24b are removed, and a funnel-shaped branch cylinder 33a is provided at the downstream end of the hollow body 34. , 33b, 33c are connected to each other,
The downstream ends of the branch ducts 3a, 33b and 33c are respectively connected to the branch ducts 10 through stop valves 23a, 23b and 23c.
a, 10b, and 10c. The branch cylinder 33
The opening area ratio of a, 33b, 33c is a burner (not shown).
Is set to a predetermined value in accordance with the amount of pulverized coal to be fed to the tank.

【0021】前記微粉炭混合器32を図1及び図2によ
り説明する。
The pulverized coal mixer 32 will be described with reference to FIGS.

【0022】微粉炭混合器32は筒状の枠体35にエレ
メント36を複数段に配設したものであり、該エレメン
ト36は枠体35の軸心に対して直交している。該エレ
メント36は微粉分散棒37を同一平面内に所要ピッチ
で平行に配設したものである。前記微粉分散棒37は例
えば断面がL字状のアングル型材が使用され、又アング
ル型材の角の稜線が粉流の上流側に位置する様に配置さ
れている。
The pulverized coal mixer 32 has a plurality of elements 36 arranged in a cylindrical frame 35 in a plurality of stages. The elements 36 are orthogonal to the axis of the frame 35. The element 36 has fine powder dispersing rods 37 arranged in parallel at a required pitch in the same plane. The fine powder dispersing rod 37 is, for example, an angle-shaped member having an L-shaped cross section, and is arranged such that the corner ridge of the angle-shaped member is located on the upstream side of the powder flow.

【0023】下から2段目の微粉分散棒37aの上側、
下側に隣接する段のエレメント36bは微粉分散棒37
bが前記微粉分散棒37aに対して直交する様に配置さ
れ、上側の隔段のエレメント36cは微粉分散棒37c
が前記微粉分散棒37aに対して平行で且つ前記微粉分
散棒37aと微粉分散棒37aとの中間に位置する様に
なっている。
Above the fine powder dispersion rod 37a in the second stage from the bottom,
The element 36b of the lower adjacent stage is a fine powder dispersion rod 37.
b is arranged so as to be orthogonal to the fine powder dispersion rod 37a, and the upper separated element 36c is arranged on the fine powder dispersion rod 37c.
Are arranged in parallel with the fine powder dispersion rod 37a and in the middle between the fine powder dispersion rod 37a and the fine powder dispersion rod 37a.

【0024】以下、作用を説明する。尚、従来と同様の
ものについては説明は省略する。
The operation will be described below. The description of the same components as those in the related art is omitted.

【0025】微粉炭ミル(図示せず)から前記一次空気
ダクト9内を流通した一次空気中の微粉炭は前記曲部2
5を通過する時に遠心力の作用により該曲部25の外周
側に偏在した状態となり、該曲部25の外周側の一次空
気中の微粉炭濃度が高い状態で前記微粉混合器32内に
流入する。
The pulverized coal in the primary air flowing from the pulverized coal mill (not shown) in the primary air duct 9 is
5, due to the action of centrifugal force, the air is unevenly distributed on the outer peripheral side of the curved portion 25, and flows into the fine powder mixer 32 in a state where the concentration of pulverized coal in the primary air on the outer peripheral side of the curved portion 25 is high. I do.

【0026】一次空気中の微粉炭は前記各微粉分散棒3
7に衝突しながら前記エレメント36を通過する。気体
搬送の粉流体が前記微粉分散棒37に衝突することで粉
流体の流れが分岐されると共に、分岐された流れは微粉
分散棒37の斜面によって流れに対して横方向に偏向さ
れて分散される。その為、微粉炭分散濃度が高い部分
は、各エレメント36を通過する毎に分散されてゆき、
微粉炭濃度が均一化される。更に、微粉炭分散濃度が高
い程、前記微粉炭分散棒37に衝突する微粉炭量が多い
ので、微粉炭分散濃度の高い部分の通過抵抗が大きくな
り、微粉炭の通過速度は微粉炭分散濃度の低い部分と比
べ遅くなる。従って、前記各エレメント36を単位時間
当りに通過する微粉炭量は次第に均一化され、該エレメ
ント36通過後の一次空気中の微粉炭は均一に分散され
た状態となる。
The pulverized coal in the primary air is supplied to each of the fine powder
7 while passing through the element 36. The flow of the powder fluid is diverged by the collision of the powder fluid of the gas transport with the fine powder dispersion rod 37, and the branched flow is deflected laterally with respect to the flow by the slope of the fine powder dispersion rod 37 and dispersed. You. Therefore, the portion where the pulverized coal dispersed concentration is high is dispersed every time when passing through each element 36,
The pulverized coal concentration is made uniform. Furthermore, as the pulverized coal dispersed concentration increases, the amount of pulverized coal colliding with the pulverized coal dispersion rod 37 increases, so that the passage resistance of the portion where the pulverized coal dispersed concentration is high increases, and the passing speed of the pulverized coal is reduced. It is slower than the lower part. Therefore, the amount of pulverized coal passing through each element 36 per unit time is gradually made uniform, and the pulverized coal in the primary air after passing through each element 36 is in a state of being uniformly dispersed.

【0027】微粉炭が均一に分散された状態の一次空気
は前記微粉炭分配器31に流入し、一次空気中の微粉炭
は前記分岐胴33a,33b,33cの開口面積比に比
例して、該各分岐ダクト10a,10b,10cに分配
され、前記各バーナ(図示せず)に所定量の微粉炭が供
給される。
The primary air in which the pulverized coal is uniformly dispersed flows into the pulverized coal distributor 31, and the pulverized coal in the primary air is proportional to the opening area ratio of the branch cylinders 33a, 33b, 33c. A predetermined amount of pulverized coal is distributed to the branch ducts 10a, 10b, and 10c, and is supplied to the burners (not shown).

【0028】尚、上記実施の形態では、前記微粉炭分散
棒37に前記L字状のアングル型材を使用したが、長尺
部材であれば傾斜させた平帯板或は丸棒等であってもよ
い。
In the above-described embodiment, the L-shaped angle-shaped member is used for the pulverized coal dispersion rod 37. However, in the case of a long member, an inclined flat band plate or round bar is used. Is also good.

【0029】[0029]

【発明の効果】以上述べた如く本発明によれば、微粉炭
混合器への流入時に一次空気中の微粉炭分散濃度が均一
でなくても、該微粉炭混合器通過中に均一になり、微粉
炭分配器内に均一に分散した一次空気を供給できる。
As described above, according to the present invention, even if the pulverized coal dispersed concentration in the primary air is not uniform when flowing into the pulverized coal mixer, it becomes uniform during the passage through the pulverized coal mixer, Primary air uniformly dispersed in the pulverized coal distributor can be supplied.

【0030】従って、均等な微粉炭の分配が確実に行え
ると共に、微粉炭分配器内に粉流体の分散状態を調整す
るダンパが不要となり、ダンパに付随する面倒な取付け
調整作業が省略でき設備コストの低減、工期の短縮が図
れるという優れた効果を発揮する。
Therefore, the pulverized coal can be evenly distributed, and a damper for adjusting the dispersion state of the pulverized fluid in the pulverized coal distributor is not required. It has the excellent effect of reducing the time and shortening the construction period.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施の形態を示す概略説明図である。FIG. 1 is a schematic explanatory view showing an embodiment of the present invention.

【図2】該実施の形態に係るエレメントを示す斜視図で
ある。
FIG. 2 is a perspective view showing an element according to the embodiment.

【図3】微粉炭焚ボイラ設備を示す系統図である。FIG. 3 is a system diagram showing a pulverized coal-fired boiler facility.

【図4】従来例を示す概略説明図である。FIG. 4 is a schematic explanatory view showing a conventional example.

【符号の説明】[Explanation of symbols]

30 微粉炭分配装置 31 微粉炭分配器 32 微粉炭混合器 36 エレメント 37 微粉分散棒 Reference Signs List 30 pulverized coal distribution device 31 pulverized coal distributor 32 pulverized coal mixer 36 element 37 pulverized dispersion rod

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 気体搬送の微粉炭粉流を複数の流れに分
岐する微粉炭分配器と該微粉炭分配器の上流側に配設さ
れた微粉炭混合器とを具備し、該微粉炭混合器が軸心と
直交するエレメントを複数段有し、該エレメントは所要
数の微粉分散棒を同一面内に平行に配設して成ることを
特徴とする微粉炭分配装置。
1. A pulverized coal distributor that branches a gas-conveyed pulverized coal powder stream into a plurality of streams, and a pulverized coal mixer disposed upstream of the pulverized coal distributor. A pulverized coal distributing apparatus characterized in that the vessel has a plurality of elements orthogonal to the axis, and the elements are provided with a required number of fine powder dispersion rods in parallel in the same plane.
【請求項2】 前記微粉分散棒の上側、下側の隣接する
段のエレメントは微粉分散棒が前記微粉分散棒に対して
直交する様に配置された請求項1の微粉炭分配装置。
2. The pulverized coal distribution apparatus according to claim 1, wherein the upper and lower adjacent elements of the fine powder dispersing rod are arranged such that the fine powder dispersing rod is orthogonal to the fine powder dispersing rod.
【請求項3】 前記微粉分散棒に対し隔段のエレメント
は該隔段の微粉分散棒が前記微粉分散棒に対して平行で
且つ前記微粉分散棒と微粉分散棒との中間に位置する請
求項1の微粉炭分配装置。
3. The fine powder dispersing rod is located at an intermediate element between the fine powder dispersing rod and the fine powder dispersing rod. 1. Pulverized coal distribution device.
JP10211224A 1998-07-27 1998-07-27 Pulverized coal distributing device Pending JP2000046315A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10211224A JP2000046315A (en) 1998-07-27 1998-07-27 Pulverized coal distributing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10211224A JP2000046315A (en) 1998-07-27 1998-07-27 Pulverized coal distributing device

Publications (1)

Publication Number Publication Date
JP2000046315A true JP2000046315A (en) 2000-02-18

Family

ID=16602351

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10211224A Pending JP2000046315A (en) 1998-07-27 1998-07-27 Pulverized coal distributing device

Country Status (1)

Country Link
JP (1) JP2000046315A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102494348A (en) * 2011-11-22 2012-06-13 闵公发 Energy-saving pulverized coal grinding and delivering equipment for boilers and kilns
JP2013544343A (en) * 2010-09-09 2013-12-12 アルストム テクノロジー リミテッド Fossil fuel distribution assembly
US9657944B2 (en) 2010-09-09 2017-05-23 General Electric Technology Gmbh Assembly for fossil fuel distribution

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013544343A (en) * 2010-09-09 2013-12-12 アルストム テクノロジー リミテッド Fossil fuel distribution assembly
US9657944B2 (en) 2010-09-09 2017-05-23 General Electric Technology Gmbh Assembly for fossil fuel distribution
CN102494348A (en) * 2011-11-22 2012-06-13 闵公发 Energy-saving pulverized coal grinding and delivering equipment for boilers and kilns
CN102494348B (en) * 2011-11-22 2014-04-16 闵公发 Energy-saving pulverized coal grinding and delivering equipment for boilers and kilns

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