JPS60114621A - Uniform distributing device of fine powdered coal in fine powdered coal burning boiler - Google Patents
Uniform distributing device of fine powdered coal in fine powdered coal burning boilerInfo
- Publication number
- JPS60114621A JPS60114621A JP22190483A JP22190483A JPS60114621A JP S60114621 A JPS60114621 A JP S60114621A JP 22190483 A JP22190483 A JP 22190483A JP 22190483 A JP22190483 A JP 22190483A JP S60114621 A JPS60114621 A JP S60114621A
- Authority
- JP
- Japan
- Prior art keywords
- flow
- fine powdered
- powdered coal
- pipe
- pulverized coal
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
Description
【発明の詳細な説明】
本釦明は微粉炭焚ボイラにおける61m粉炭バーナへの
倣粉戻供鞄鼠を均一に分配する、いわゆる微粉炭分配装
置に関するものである。微粉炭をボイラの谷倣vj炭バ
ーナへ均−区分配することの本要性は上記にある。DETAILED DESCRIPTION OF THE INVENTION This invention relates to a so-called pulverized coal distributing device that uniformly distributes a 61 m pulverized coal burner in a pulverized coal-fired boiler. The essential importance of evenly distributing pulverized coal to the valley-shaped VJ coal burner of the boiler is as described above.
(1)窒素酸化物(NOX)排出量の低減近来、NOX
排出嵐を低娯させることは国民uソ課題であり、環境−
顯としては故大島心事のひとつである。微粉炭焚ボイラ
よりのN(JX排出凰の増加は微粉炭分配の不〜−に係
る要素がIPmに多いため、本先明による微粉炭の〜−
分配装には微粉炭焚ボイラのN<)X低敵對策どしてに
要m境設備である。(1) Recent reduction in nitrogen oxide (NOX) emissions, NOX
Reducing emissions storms is a national issue and an environmental concern.
As for his face, it is one of those of the late Shinji Oshima. The increase in N (JX emissions) from pulverized coal-fired boilers is due to the fact that IPm has many factors related to poor pulverized coal distribution.
The distribution system is a pulverized coal-fired boiler, which is required to have a low resistance to N<)X.
(2)ボイラ効率の同上
微粉炭−が不均一に分配された場合、ボイラの谷バーナ
のを燃比率が乱れ、窒諷過刺燃焼のバーナと′2I!気
不足燃焼のバーナを生じ、ボイラ効率が低重する。又望
屹比奎の乱れにより、本然タストの発庄麓が増加するた
め、このタストのボイラチー−ブ付肴旅が増加し、この
曲からもボイラ効率の低重を招(。したがって不光明の
領粉炭均−分配装搬はボイラ効率の同上からも凰要設備
である。(2) If pulverized coal is distributed unevenly in the boiler efficiency, the fuel ratio in the valley burner of the boiler will be disturbed, resulting in a burner with nitrous combustion and '2I! This causes a burner with insufficient combustion, resulting in low boiler efficiency. In addition, due to the disturbance of Botan Hikyi, the number of starting points of the original tast increases, so the number of side trips with boiler-chive of this tast increases, and this song also causes a decrease in boiler efficiency. The pulverized coal leveling and distribution equipment is essential equipment from the standpoint of boiler efficiency as well.
(3)ボイラチーーブおよびバーナ廻り部品の耐用年数
の1−上
微粉炭が不均一に分配された揚台、上記(2)の如く空
燃比率の乱れにより、微粉炭の燃焼温良が谷バーナによ
り簡低を生じる。この結果、鍋温部分のボイラチューブ
及びバーナ廻り部品の耐用年数が低下する。仁の、に味
から微粉炭を均一分配し、均一な燃焼m反を得る仁とは
車装である。(3) The service life of the boiler chive and parts around the burner is shortened due to the lifting platform where the pulverized coal is distributed unevenly, and the air-fuel ratio being disturbed as described in (2) above. Produces low. As a result, the service life of the boiler tube in the pot heating section and parts around the burner is reduced. Kernel is used to distribute pulverized coal evenly and achieve uniform combustion.
(4)ボイラ内11火物のH用年歓の同上上記(3ンと
同じ坂出により、微粉炭の不均一分配はボイラ内1大物
のH用年畝を著しく低下させる。征りて傾粉灰の均−分
配装置は向J大物の耐用年数のN上からもに要設備であ
る。(4) Same as above for 11 fires in the boiler. An ash equalization and distribution device is a necessary piece of equipment in order to extend the service life of a large-scale plant.
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、A1!境曲、1工ネルキー曲及び装置保全の血
から非市にJk東な仁とであることがわかる。なおここ
ηいう均一分配とはム鰍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。As described above, uniformly distributing pulverized coal to each burner of the boiler is A1! It can be seen from the blood of Kyoto music, 1st grade Nerky music, and equipment maintenance that he is a JK Higashi Jin. Note that the uniform distribution η here refers to not only the uniform distribution of mussels, but also the uniform distribution of mussels.
It also includes the meaning of uniform distribution of particle size.
微粉炭は石炭粉砕機(ミルフにより200メノンニアン
ターが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hpA粉砕軸(εルプ出口より1基の分配器につき通
′M2〜4本のバーナへ分配される。又ボイラ負匈の増
減や、MTo時又は停止時に分配器の場w4皆行う場合
がある。石炭粉砕機(ミルノから各バーナ迄は微粉次官
内を3aI?g80〜49 m/aの流速にて空気軛送
されている。The pulverized coal is pulverized by a coal pulverizer (milf) until it is pulverized to 80% or more, and then sent by air to each burner of the boiler for pulverized coal combustion.The pulverized coal is It is distributed to M2 to 4 burners per distributor.In addition, it may be necessary to increase/decrease the boiler load, or at the time of MTo or stoppage.Coal crusher (from Milno to Up to each burner, air is fed through the fine powder chamber at a flow rate of 3aI?g80 to 49 m/a.
本発明はnu述した如く微粉炭バーナにおいて秘めてム
要な微粉炭の均一分配をiJ餌とした実用価値の^い微
粉炭焚ボイラにおける微粉炭の均−分配装諏を提供せん
とするものである。As mentioned above, the present invention aims to provide a device for evenly distributing pulverized coal in a pulverized coal-fired boiler, which has practical value and uses the uniform distribution of pulverized coal, which is a hidden and important issue in a pulverized coal burner, as a bait. It is.
本発明による微粉炭の均一分配原理はall記微粉炭管
の途中に曲物部(ペンド部フを設は微粉炭の慣性力(1
nerLia )及び遠心力を利用してf&粉炭管内の
外流血に微粉炭を偏流させて後、必要数の仕切板を有し
た分配器により均一分配するも0である。以)実施例を
内向に基いて説明する。The principle of uniform distribution of pulverized coal according to the present invention is as follows: The inertia of pulverized coal (1
nerLia) and centrifugal force to divert the pulverized coal to the external flow inside the f& pulverized coal pipe, and then uniformly distribute it using a distributor having the required number of partition plates. Below) Examples will be explained based on introversion.
gi4117に示す如く石炭粉砕機(ミル)(υ出口の
微粉次官(2)内の微粉炭と空気の固気2相流は同転流
等の、IP整流となっているため、整流器(3)により
整流し胆線流とする。又微粉次官(2Jは適冷円形であ
るため、西角管(4)を設けて角官とする。この後に8
06〜90°の適当な角度を自した偏流管(5)を設け
て上記固気2相流を偏流させる。内気2相流中の微粉炭
はその具比嵐が2.0〜2.8と堅気より凰いため、慣
性力(1nertia )及び庖むカにより偏流−(5
)の外面に偏った流れとなる。微粉炭が均一偏流となっ
たところで分配器(6)にて分配する。微粉炭と望気の
流れを第4因に示している。分配器は通富2〜4である
が彫2凶は8分配の場合の分配器を示す。第8因は分配
管の171線における断面−を示す。カットダンパ(7
) 、 L8J 、 (9月よ通N鮨とするが、ボイラ
の負萄変kJJ等により、上Hdカットダンパの内1個
又は2個を開とする揚台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。As shown in gi4117, the solid-gas two-phase flow of pulverized coal and air in the coal crusher (mill) (υ outlet pulverizer (2) is IP rectified, such as simultaneous commutation, so the rectifier (3) It is rectified and made into a biliary flow.Also, since 2J is a circular shape suitable for cooling, a west angle pipe (4) is installed to make it a square flow.After this, 8
A deflection tube (5) having an appropriate angle of 06 to 90 degrees is provided to deflect the solid-gas two-phase flow. Pulverized coal in a two-phase internal air flow has a specific storm ratio of 2.0 to 2.8, which is lower than that of solid air, so the inertia force (1nertia) and the swallowing force cause drifting - (5
) The flow is biased towards the outer surface of the area. When the pulverized coal becomes uniformly distributed, it is distributed by a distributor (6). The flow of pulverized coal and desired air is shown as the fourth factor. The distributor is Tsutomi 2 to 4, but Hori 2 Kyo shows the distributor for 8 distributions. The eighth factor shows the cross section of the distribution pipe at line 171. Cut damper (7
) , L8J , (September 2019), but due to boiler negative changes kJJ, etc., there is a platform where one or two of the upper Hd cut dampers are opened, but even in this case, the distribution efficiency is Must be in good condition.
次に8分配の場合の本発明にょる微粉炭分配装置の分配
効率のテストデータを示す。Next, test data on the distribution efficiency of the pulverized coal distribution device according to the present invention in the case of 8 distributions will be shown.
(1)8分配の分配効率(カントタンパ<7) 、 (
8)・(9)全一ノ
(2)2分配の分配効率(カットタンパ(7)貼、カッ
トタンパ(8)、 (9)全開ン
余分配剤率とは完全に等分配された場合をioo%とす
る。(1) Distribution efficiency of 8 distribution (canto tamp < 7), (
8)・(9) Total one-(2) Distribution efficiency of two distributions (Cut tamper (7) pasted, Cut tamper (8), (9) Full open excess distribution rate refers to the case of completely equal distribution. Let it be ioo%.
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
タを下記に示す。Also, test data on pressure drop of the pulverized coal distribution device according to the present invention is shown below.
(3)8分配の圧力損失(カットタンパ(7) 、 (
8) 、 (9少全(4)2分配の圧力損失(カットタ
ンパ<711&j、カット以上の緑に本発明による緻粉
炭の均一分配装置は従米の分配表鈑と比較rると1記の
恢れた効果がある。(3) Pressure loss of 8 distribution (cut tamper (7), (
8), (9 small total (4) Pressure loss of 2 distribution (cut tamper < 711 & j, cut or more green) The uniform distribution device of the pulverized coal according to the present invention has the following results when compared with the conventional distribution plate. It has a strong effect.
(1) 例えは従米のベンチュリータイプの分配装置は
偵初炭旨ぬ使の10倍以上の並鹿々営部を必要とするが
本発明による愉流普タイプの分配装置はui*都を必要
としy7いため、設籠上、+を二重に有ホUである。(1) For example, the Venturi-type dispensing device of Jubai requires more than 10 times as much Namikaka-eibu as the Reichu Tan Umunushi, but the Yuryu Fu-type dispensing device of the present invention requires ui*capital. Since it is y7, the + is doubled in the construction.
(2) 不発1による分配装置はl#造が量率であるた
め従米タイプに比較して比力損失が1/2〜l/jlと
少い。従って微粉炭輸送用空気の辻力が少(でよいため
、大きな送風設備を必要としない。(2) Since the distribution device based on the misexplosion 1 has a quantity rate of 1#, the specific force loss is small at 1/2 to 1/jl compared to the conventional type. Therefore, only a small amount of force is required for transporting the pulverized coal, so large air blowing equipment is not required.
(3) 分配効率については従米タイプが40〜80%
であるのに比軟して本発明による分配装置の分子16T
h亭は冨に90%台の効率を維持できる。(3) Distribution efficiency is 40-80% for the rice-based type.
In comparison, the molecule 16T of the dispensing device according to the invention is
H-tei can maintain an efficiency of 90%.
第1図は本発明の微粉炭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IIO凶、第2図は同実施カの
分配器のm愈を示す睨明図、第81は第21の1−1m
における断i10図、第4図は本実施例での微粉炭と空
気の流れを示す睨明凶て71)。
(υ:而面粉砕機−(ミルク
(2ン:微粉R官(3フ:Mm器
(4):円周w(5):偏m官
(bJ:分配器 <7) 、 (8) 、を旬:カット
タンパ第1図
第2図
1 1
第3図
第4図Fig. 1 is an illustration showing an example of the uniform distribution device for pulverized coal in a pulverized coal boiler of the present invention, Fig. 2 is a perspective view showing the discharge of the distributor of the same embodiment, and Fig. 1-1m
10 and 4 are cross-sectional views showing the flow of pulverized coal and air in this example (71). (υ: Surface crusher - (milk (2): Fine powder R (3): Mm (4): Circumference w (5): Partial m (bJ: Distributor <7), (8), Season: Cut Tampa Figure 1 Figure 2 Figure 1 1 Figure 3 Figure 4
Claims (1)
を菟気輔送する微粉炭柚込Il!1)島中に80〜90
°の任忽な角度を有する角型ベンド状の偏泥自を設けて
窒気輛送中の微粉炭を慣性力と遠心力により偏流さ♂、
―偏流官の用u側に接続した分配器により偏九した微粉
炭を仕思数に勾−に分配することを狩偵とする微粉pA
焚ホボイにおける@l初仄の均一分配装置。1) In a pulverized coal-fired boiler, pulverized coal is transported to the burner of the boiler. 1) 80-90 throughout the island
A rectangular bend-shaped sludge with an arbitrary angle of ° is installed to deflect the pulverized coal during nitrogen transport by inertial force and centrifugal force.
- Fine powder pA whose purpose is to distribute the biased pulverized coal according to the number of gradients using a distributor connected to the U side of the flow distribution officer.
The first uniform distribution device in the firing hoboi.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22190483A JPS60114621A (en) | 1983-11-24 | 1983-11-24 | Uniform distributing device of fine powdered coal in fine powdered coal burning boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22190483A JPS60114621A (en) | 1983-11-24 | 1983-11-24 | Uniform distributing device of fine powdered coal in fine powdered coal burning boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60114621A true JPS60114621A (en) | 1985-06-21 |
Family
ID=16773976
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22190483A Pending JPS60114621A (en) | 1983-11-24 | 1983-11-24 | Uniform distributing device of fine powdered coal in fine powdered coal burning boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60114621A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1418383A1 (en) * | 2001-12-03 | 2004-05-12 | Babcock-Hitachi Kabushiki Kaisha | FUEL DISTRIBUTION DEVICE FOR FUEL FEED DUCTS, AND METHOD OF OPERATING THE DISTRIBUTION DEVICE |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56141232A (en) * | 1980-04-05 | 1981-11-04 | Kawasaki Heavy Ind Ltd | Distribution method for particles in gas current and device thereof |
JPS58110908A (en) * | 1981-12-17 | 1983-07-01 | コンバツシヨン・エンヂニアリング・インコ−ポレ−テツド | Burner |
-
1983
- 1983-11-24 JP JP22190483A patent/JPS60114621A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56141232A (en) * | 1980-04-05 | 1981-11-04 | Kawasaki Heavy Ind Ltd | Distribution method for particles in gas current and device thereof |
JPS58110908A (en) * | 1981-12-17 | 1983-07-01 | コンバツシヨン・エンヂニアリング・インコ−ポレ−テツド | Burner |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1418383A1 (en) * | 2001-12-03 | 2004-05-12 | Babcock-Hitachi Kabushiki Kaisha | FUEL DISTRIBUTION DEVICE FOR FUEL FEED DUCTS, AND METHOD OF OPERATING THE DISTRIBUTION DEVICE |
EP1418383A4 (en) * | 2001-12-03 | 2008-01-23 | Babcock Hitachi Kk | Fuel distribution device for fuel feed ducts, and method of operating the distribution device |
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