JPH0490412A - Pulverized coal distributor - Google Patents
Pulverized coal distributorInfo
- Publication number
- JPH0490412A JPH0490412A JP20682090A JP20682090A JPH0490412A JP H0490412 A JPH0490412 A JP H0490412A JP 20682090 A JP20682090 A JP 20682090A JP 20682090 A JP20682090 A JP 20682090A JP H0490412 A JPH0490412 A JP H0490412A
- Authority
- JP
- Japan
- Prior art keywords
- pulverized coal
- pipes
- coal
- concentration
- pipe
- 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
Links
- 239000003245 coal Substances 0.000 title claims abstract description 65
- 238000005119 centrifugation Methods 0.000 abstract description 4
- 238000002485 combustion reaction Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、微粉炭焚きボイラに適用される微粉炭分配装
置に関し、更に詳しくは燃焼効率の改善を図った微粉炭
分配装置に関する
従来の技術
第4図は、従来より用いられている微粉炭焚きボイラの
構成を示す斜視図である。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a pulverized coal distribution device applied to a pulverized coal-fired boiler, and more specifically relates to a pulverized coal distribution device designed to improve combustion efficiency. The figure is a perspective view showing the configuration of a conventionally used pulverized coal-fired boiler.
第4図において、1は火炉2を有する微粉炭焚きボイラ
、3は石炭粉砕機であり、石炭投入口4から投入される
石炭(図示せず)を粉砕する。また、5はファンであり
、送風管6を介して図示しない加熱装置で加熱した熱空
気を石炭粉砕機3に送風する。そして、7a〜7eは直
管、8a〜8eはベント管、9は微粉炭バーナ、IOは
火炎である。In FIG. 4, 1 is a pulverized coal-fired boiler having a furnace 2, and 3 is a coal crusher, which crushes coal (not shown) introduced from a coal input port 4. Further, 5 is a fan, which blows hot air heated by a heating device (not shown) to the coal crusher 3 through an air pipe 6. Further, 7a to 7e are straight pipes, 8a to 8e are vent pipes, 9 is a pulverized coal burner, and IO is a flame.
上記の構成において、石炭投入口4から投入された石炭
は、石炭粉砕機3で粉砕され、ファン5を介して送風さ
れる熱空気により直管7(7a〜7e)及びベント管8
(88〜8e)を介して矢印aで示す経路に従って気流
搬送される。そして、この搬送された微粉炭は、微粉炭
焚きボイラ1の火炉2の各コーナ部に設けられた微粉炭
バーナ9にて火炉2内に投入され燃焼される。In the above configuration, the coal input from the coal input port 4 is crushed by the coal crusher 3, and heated by hot air blown through the fan 5 into the straight pipes 7 (7a to 7e) and the vent pipe 8.
(88 to 8e) and is transported by air flow along the path indicated by arrow a. The transported pulverized coal is then charged into the furnace 2 and burned by pulverized coal burners 9 provided at each corner of the furnace 2 of the pulverized coal-fired boiler 1.
発明が解決しようとする課題
ところで、このよろな微粉炭焚きボイラにおいては、一
般に石炭と空気の比率は1:2〜1:5程度であり、特
にボイラ負荷の低い燃焼石炭量の少ないときは空気の比
率か大きくなる。そして、バーナ9から噴射される微粉
炭は空気の割合か大きくなると、火炎10の着火が火炉
2の内部へ飛び不安定燃焼を起こす。Problems to be Solved by the Invention By the way, in these various types of pulverized coal-fired boilers, the ratio of coal to air is generally about 1:2 to 1:5, and especially when the boiler load is low and the amount of combustion coal is small, air The ratio of When the proportion of air in the pulverized coal injected from the burner 9 increases, the flame 10 ignites into the furnace 2, causing unstable combustion.
第5図は、この不安定燃焼の問題を解決した従来技術を
示す断面図である。FIG. 5 is a sectional view showing a conventional technique that solves this problem of unstable combustion.
即ち、従来は、微粉炭バーナ9の内部に微粉炭分離装置
t11を設け、遠心力分離またはサイクロンを利用して
高濃度の微粉体空気混合体と低濃度の微粉炭空気混合体
とに分けている。この結果、濃い微粉炭バーナ9aでの
火炎が淡い微粉炭バーナ9bの助炎バーナとなり、濃淡
バーナ全体が安定燃焼することになる。That is, conventionally, a pulverized coal separator t11 is provided inside the pulverized coal burner 9, and a pulverized coal air mixture with a high concentration and a pulverized coal air mixture with a low concentration are separated using centrifugal force separation or a cyclone. There is. As a result, the flame in the dense pulverized coal burner 9a becomes an auxiliary flame in the light pulverized coal burner 9b, resulting in stable combustion in the entire concentrated burner.
しかしながら、上記従来の微粉炭分離装置11のみでは
充分に石炭/空気比の高いものを得ることは難しく、よ
り効果的に遠心力分離またはサイクロン効果を得るため
には流体圧損を大きくして対応しなければならないとい
う問題があった。However, it is difficult to obtain a sufficiently high coal/air ratio using only the conventional pulverized coal separation device 11, and in order to obtain more effective centrifugal force separation or cyclone effect, it is necessary to increase the fluid pressure drop. There was a problem that it had to be done.
本発明は、このような従来技術の課題を解決するために
なされたもので、流体圧損か従来と同程度で高濃度の微
粉炭を得ることが可能な微粉炭分配装置を提供すること
を目的とする。The present invention was made in order to solve the problems of the prior art, and an object of the present invention is to provide a pulverized coal distribution device that can obtain pulverized coal at a high concentration with a fluid pressure drop comparable to that of the conventional technology. shall be.
課題を解決するための手段
上記の課題を解決するために、本発明は、石炭粉砕機で
粉砕された微粉炭を、少なくとも2個のベント管と、こ
れらのベント管の間を接続する直管および微粉炭バーナ
を介して微粉炭焚きボイラに気流搬送する微粉炭分配装
置において、前記ベント管の少なくとも一端側の接続口
を二股とし、この二股接続口をベント管の内周及び外周
に形成すると共にベント管の途中で合流するように形成
し、前記2個のベント管の内周及び外周の二股接続口同
志を2本の直管を用いて接続したものである。Means for Solving the Problems In order to solve the above problems, the present invention provides pulverized coal that has been pulverized by a coal pulverizer through at least two vent pipes and a straight pipe connecting these vent pipes. and a pulverized coal distribution device that air-flows the pulverized coal to a pulverized coal-fired boiler via a pulverized coal burner, wherein at least one end side of the vent pipe has a bifurcated connection port, and the bifurcated connection port is formed on the inner and outer peripheries of the vent pipe. The vent pipes are formed so as to merge in the middle of the vent pipes, and the bifurcated connection ports on the inner and outer circumferences of the two vent pipes are connected using two straight pipes.
作用
上記の手段によれば、気流搬送される微粉炭は、ベント
管を通過する際に遠心分離により外周部を通過する気流
に含まれる微粉炭の濃度が内周部を通過する気流に含ま
れる微粉炭の濃度より高濃度となる。そして、これらの
気流は直管で別々に搬送され、次段のベント管で更に濃
淡の度合いが強くなる。Effect: According to the above means, the pulverized coal transported by air current is centrifuged when passing through the vent pipe, so that the concentration of pulverized coal contained in the air flow passing through the outer circumference is contained in the air flow passing through the inner circumference. The concentration is higher than that of pulverized coal. These airflows are then conveyed separately through straight pipes, and the degree of density becomes even stronger in the next-stage vent pipe.
実施例
以下、図面を参照して本発明の実施例について詳述する
。Embodiments Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
第1図は本発明の一実施例を示す微粉炭分配装置の要部
を示す斜視図、第2図は一端のみか二股接続口に形成さ
れたベント管の斜視図、第3図は両端がそれぞれ二股接
続口に形成されたベント管の斜視図である。FIG. 1 is a perspective view showing the main parts of a pulverized coal distribution device showing an embodiment of the present invention, FIG. It is a perspective view of the vent pipe formed in each bifurcated connection port.
先ず第2図において、ベント管12はほぼ直角に曲げら
れて、一端が単一の大径接続口12aとされ、かつ他端
が二股接続口12b、12cとされて、直角部の外周及
び内周側に形成されている。そして、これらの二股接続
口12b、12cの仕切り12dはベンド管12の途中
まで形成され、これにより二股の接続口12bと12c
とはベント管12の途中で合流されている。First, in FIG. 2, the vent pipe 12 is bent almost at a right angle, with one end having a single large-diameter connection port 12a, and the other end having bifurcated connection ports 12b and 12c. It is formed on the circumferential side. The partition 12d between these bifurcated connection ports 12b and 12c is formed up to the middle of the bend pipe 12, so that the bifurcated connection ports 12b and 12c
and are merged in the middle of the vent pipe 12.
次に、第3図はほぼ直角に曲げられたベント管12’の
両端がそれぞれ二股接続口12b、12cに形成された
もので、第2図と同様にこれらの二股接続口12b、1
2cの仕切り12dはベンド管12′の途中まで形成さ
れ、これにより二股の接続口12b′ と12c’とは
ベント管12′の途中で合流されている。Next, in FIG. 3, both ends of a vent pipe 12' bent at a substantially right angle are formed into bifurcated connection ports 12b and 12c, respectively, and similarly to FIG. 2, these bifurcated connection ports 12b and 1
The partition 12d of 2c is formed up to the middle of the bend pipe 12', so that the bifurcated connection ports 12b' and 12c' are joined in the middle of the vent pipe 12'.
そして、第1図は直管7と、上記したベント管12.1
2’ と、直管13.13’ とを組み合わせて微粉炭
分配装置を構成した状態を示すもので、直管13はベン
ト管12.12’の二股の外周接続口12b同志を、ま
た直管13′はベント管12.12’の二股の内周接続
口12c同志をそれぞれ接続している。FIG. 1 shows the straight pipe 7 and the above-mentioned vent pipe 12.1.
2' and a straight pipe 13.13' are combined to form a pulverized coal distribution device. 13' connects the bifurcated inner peripheral connection ports 12c of the vent pipes 12 and 12', respectively.
上記の構成によれば、石炭粉砕機3(第4図参照)によ
り粉砕された石炭は、直管7を介してベント管12に搬
送され、矢印a、とa!の方向に分離される。この場合
、微粉炭は遠心分離によりベント管12の外周側の矢印
a1を通る方の濃度が高く、ベント管12の内周側の矢
印a、を通る方の濃度が低くなる。そして、これら濃淡
の微粉炭は直管13.13’により別々に搬送されてベ
ント管12’に入り、矢印alv 84+ a8の
方向に進む。そして、ここでも同様の遠心分離により更
に濃淡の度合いが促進される。このように高い濃度と低
い濃度に分離された微粉炭は火炉2(第4図及び第5図
参照)に搬送されて燃焼するか、濃い微粉炭の火炎が淡
い微粉炭バーナの助炎バーナとなり、濃淡バーナ全体が
安定燃焼する。According to the above configuration, the coal crushed by the coal crusher 3 (see FIG. 4) is conveyed to the vent pipe 12 via the straight pipe 7, and the coal is conveyed to the vent pipe 12 by the arrows a and a! separated in the direction of In this case, the concentration of pulverized coal is higher in the direction passing through the arrow a1 on the outer circumference side of the vent pipe 12 due to centrifugation, and the concentration in the direction passing through the arrow a on the inner circumference side of the vent pipe 12 is lower. These concentrated and light pulverized coals are conveyed separately by the straight pipes 13 and 13', enter the vent pipe 12', and advance in the direction of the arrow alv 84+a8. Here, too, the degree of shading is further promoted by similar centrifugation. The pulverized coal separated into high and low concentrations is transported to the furnace 2 (see Figures 4 and 5) and burned, or the flame of the dense pulverized coal becomes an auxiliary flame of the lighter pulverized coal burner. , the entire concentration burner burns stably.
なお、本実施例においては、ベント管の数を2個として
示したが、ベント管の数を多くすることにより濃淡の度
合いを更に高めることができる。In this embodiment, the number of vent pipes is two, but the degree of shading can be further increased by increasing the number of vent pipes.
また、ベント管の形状は図示の例に限ることなく種々設
計することができる。Further, the shape of the vent pipe is not limited to the illustrated example, and various designs can be made.
発明の効果
以上述べたように、本発明によれば、微粉炭焚きボイラ
に適用される微粉炭分配装置におけるベント管の少なく
とも一端側の接続口を二股とし、この二股接続口をベン
ト管の内周及び外周に形成すると共にベント管の途中で
合流するように形成し、前記2個のベント管の内周及び
外周の二股接続口同志を2本の直管を用いて接続したの
で、微粉炭はこれらの中を搬送される途中で濃度の高い
部分と低い部分に分離されて火炉に達すAoその結果、
バーナの着火点が安定し、未燃燐分の少ない燃焼を得る
ことができる。また、特に石炭/空気比率の低くなるボ
イラ低負荷時にも、濃度の高い微粉炭の固気流体が得ら
れるため燃焼状態が安定しボイラの低負荷運転が可能と
なり、省エネルギー化を図ることができる。Effects of the Invention As described above, according to the present invention, the connection port on at least one end side of the vent pipe in a pulverized coal distribution device applied to a pulverized coal-fired boiler is bifurcated, and the bifurcated connection port is connected to the inside of the vent pipe. The pulverized coal As it is transported through these, it is separated into high-concentration parts and low-concentration parts and reaches the furnace.As a result,
The ignition point of the burner is stabilized, and combustion with less unburned phosphorus can be achieved. In addition, even when the boiler is under low load, especially when the coal/air ratio is low, a highly concentrated pulverized coal solid fluid can be obtained, which stabilizes the combustion state and enables the boiler to operate at low load, resulting in energy savings. .
第1図は本発明による微粉炭分配装置の一例を示す要部
の斜視図、第2図及び第3図はその2個のベント管を示
す斜視図、第4図は従来の微粉炭分配装置の全体構成を
示す斜視図、第5図はその一部分の断面図である。
1・・微粉炭焚きボイラ、2・・火炉、3・・石炭粉砕
機、7・・直管、9・・微粉炭バーナ、1242’
・・ベント管、12b、 12c・・二股接続口、12
d・・仕切り、13.13′ ・・直管。FIG. 1 is a perspective view of essential parts showing an example of a pulverized coal distribution device according to the present invention, FIGS. 2 and 3 are perspective views showing two vent pipes thereof, and FIG. 4 is a conventional pulverized coal distribution device. FIG. 5 is a perspective view showing the overall structure of the device, and FIG. 5 is a sectional view of a portion thereof. 1.Pulverized coal-fired boiler, 2.Furnace, 3.Coal crusher, 7.Straight pipe, 9.Pulverized coal burner, 1242'
...Bent pipe, 12b, 12c...Two-pronged connection port, 12
d...Partition, 13.13'...Straight pipe.
Claims (1)
ベント管と、これらのベント管の間を接続する直管およ
び微粉炭バーナを介して微粉炭焚きボイラに気流搬送す
る微粉炭分配装置において、前記ベント管の少なくとも
一端側の接続口を二股とし、この二股接続口をベント管
の内周及び外周に形成すると共にベント管の途中で合流
するように形成し、前記2個のベント管の内周及び外周
の二股接続口同志を2本の直管を用いて接続したことを
特徴とする微粉炭分配装置。In a pulverized coal distribution device that airflow conveys pulverized coal pulverized by a coal crusher to a pulverized coal-fired boiler through at least two vent pipes, a straight pipe connecting these vent pipes, and a pulverized coal burner. , the connection port on at least one end side of the vent pipe is bifurcated, the bifurcated connection port is formed on the inner circumference and the outer circumference of the vent pipe, and is formed so as to join in the middle of the vent pipe, and the two vent pipes A pulverized coal distribution device characterized in that the inner and outer bifurcated connection ports are connected using two straight pipes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20682090A JPH0490412A (en) | 1990-08-06 | 1990-08-06 | Pulverized coal distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20682090A JPH0490412A (en) | 1990-08-06 | 1990-08-06 | Pulverized coal distributor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0490412A true JPH0490412A (en) | 1992-03-24 |
Family
ID=16529630
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20682090A Pending JPH0490412A (en) | 1990-08-06 | 1990-08-06 | Pulverized coal distributor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0490412A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009192204A (en) * | 2008-02-18 | 2009-08-27 | Mitsubishi Heavy Ind Ltd | Burner structure |
CN108224416A (en) * | 2018-01-18 | 2018-06-29 | 王志远 | Burner |
US11202723B2 (en) | 2016-07-01 | 2021-12-21 | The Procter & Gamble Company | Absorbent articles with improved topsheet dryness |
-
1990
- 1990-08-06 JP JP20682090A patent/JPH0490412A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009192204A (en) * | 2008-02-18 | 2009-08-27 | Mitsubishi Heavy Ind Ltd | Burner structure |
US11202723B2 (en) | 2016-07-01 | 2021-12-21 | The Procter & Gamble Company | Absorbent articles with improved topsheet dryness |
CN108224416A (en) * | 2018-01-18 | 2018-06-29 | 王志远 | Burner |
CN108224416B (en) * | 2018-01-18 | 2020-01-03 | 王志远 | Burner with a burner head |
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