JP2781222B2 - Pulverized coal combustion equipment - Google Patents

Pulverized coal combustion equipment

Info

Publication number
JP2781222B2
JP2781222B2 JP1246400A JP24640089A JP2781222B2 JP 2781222 B2 JP2781222 B2 JP 2781222B2 JP 1246400 A JP1246400 A JP 1246400A JP 24640089 A JP24640089 A JP 24640089A JP 2781222 B2 JP2781222 B2 JP 2781222B2
Authority
JP
Japan
Prior art keywords
pulverized coal
concentration
air
pipeline
flame holding
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 - Fee Related
Application number
JP1246400A
Other languages
Japanese (ja)
Other versions
JPH03110308A (en
Inventor
公治 倉増
茂樹 森田
成人 中下
正 神保
Original Assignee
バブコツク日立株式会社
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 バブコツク日立株式会社 filed Critical バブコツク日立株式会社
Priority to JP1246400A priority Critical patent/JP2781222B2/en
Publication of JPH03110308A publication Critical patent/JPH03110308A/en
Application granted granted Critical
Publication of JP2781222B2 publication Critical patent/JP2781222B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は微粉炭燃焼装置に係り、特に火炎の安定性を
向上させるのに好適な微粉炭の燃焼装置に関する。
Description: TECHNICAL FIELD The present invention relates to a pulverized coal combustion apparatus, and more particularly to a pulverized coal combustion apparatus suitable for improving flame stability.

〔従来の技術〕[Conventional technology]

従来の微粉炭燃焼装置において、例えば第5図に示す
ごとく、バーナ先端部からの逆火を防ぐ目的で、微粉炭
供給管路の搬送空気の流速を上げるために1次空気スリ
ーブ11内にベンチュリ15を設けていた。しかし、このベ
ンチュリ15の作用により、空気および微粉炭の流れが1
次空気スリーブ11の中心部に集まり、微粉炭の放出端に
設けられた保炎リング6近傍の微粉炭濃度が低下し、保
炎性を向上させ安定した火炎(特に低負荷時)を得るこ
とについての配慮は全くなされていなかった。
In a conventional pulverized coal combustion apparatus, for example, as shown in FIG. 5, in order to prevent flashback from the tip of the burner, a venturi is provided in the primary air sleeve 11 to increase the flow velocity of the conveying air in the pulverized coal supply line. 15 were provided. However, due to the action of the venturi 15, the flow of air and pulverized coal is reduced by one.
The concentration of pulverized coal near the flame holding ring 6 provided at the discharge end of pulverized coal gathers at the center of the next air sleeve 11 to improve the flame holding property and obtain a stable flame (particularly at low load). No consideration was given to it.

このため、本考案者らは実開昭63−23516号公報にお
いて、微粉炭供給管路のベンチュリの後流に微粉炭の案
内部材を設けて管壁付近で微粉炭濃度が高くなるように
し、かつ空気は整流部材により管路の半径方向における
流速がほぼ一定になる微粉炭供給装置を提案した。しか
し、低負荷燃焼時における微粉炭濃度が低い場合などに
おいて、微粉炭濃度を有効な濃度に調整し、保炎性を向
上させて安定した火炎を得る点については、いまだ十分
に満足されるものではなかった。
For this reason, the present inventors, in Japanese Utility Model Laid-Open No. 63-23516, provided a pulverized coal guide member downstream of the venturi in the pulverized coal supply pipeline so that the pulverized coal concentration becomes high near the pipe wall, In addition, a pulverized coal feeder is proposed in which the flow rate of air in the radial direction of the pipeline is substantially constant by the rectifying member. However, when the pulverized coal concentration during low load combustion is low, the point of adjusting the pulverized coal concentration to an effective concentration and improving the flame holding properties to obtain a stable flame is still sufficiently satisfactory. Was not.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

上述したごとく従来技術においては、1次空気と共に
微粉炭を供給する管路に設けられたベンチュリによる微
粉炭の偏流、すなわち、1次空気スリーブの中心付近の
微粉炭濃度が高くなることにより、その結果として1次
空気スリーブの内壁付近の微粉炭濃度が低くなり、初期
着火に必要な保炎リング近傍への有効な濃度の微粉炭を
供給するという点についての配慮はなされておらず、特
に低負荷時(微粉炭供給混合気の微粉炭濃度が低い場
合)の保炎性については十分でなく問題があった。
As described above, in the prior art, the drift of the pulverized coal by the venturi provided in the pipe that supplies the pulverized coal together with the primary air, that is, the pulverized coal concentration near the center of the primary air sleeve increases, thereby increasing the pulverized coal concentration. As a result, the concentration of pulverized coal near the inner wall of the primary air sleeve is reduced, and no consideration is given to supplying an effective concentration of pulverized coal to the vicinity of the flame holding ring required for initial ignition. When loaded (when the pulverized coal concentration of the pulverized coal supply air-fuel mixture is low), the flame holding properties are not sufficient and there is a problem.

本発明の目的は、微粉炭供給管の放出端における空気
流速および微粉炭濃度を、低負荷時においても効果的に
調整し、上記従来技術における問題点を無くすることに
より、微粉炭濃度が低い場合であってもバーナの保炎性
を向上させ、火炎の安定化をはかる微粉炭燃焼装置を提
供することにある。
An object of the present invention is to reduce the pulverized coal concentration by effectively adjusting the air flow rate and the pulverized coal concentration at the discharge end of the pulverized coal supply pipe even at a low load, and eliminating the problems in the prior art. Even in such a case, it is an object of the present invention to provide a pulverized coal combustion apparatus which improves the flame holding property of a burner and stabilizes a flame.

〔課題を解決するための手段〕[Means for solving the problem]

上記本発明の目的は、微粉炭供給管路内に設置位置の
調整が可能な微粉炭の分級エレメントと、管路の半径方
向の空気流速をほぼ一定にする案内管を設け、微粉炭濃
度が低い場合であっても上記分級エレメントの設置位置
を調整することにより管路の半径方向の空気流速分布
と、微粉炭濃度分布を最適な状態に調整することができ
る微粉炭供給装置とすることにより達成される。
The object of the present invention is to provide a pulverized coal classification element whose installation position can be adjusted in a pulverized coal supply pipe, and a guide pipe that makes the air flow velocity in the pipe radial direction substantially constant, so that the pulverized coal concentration is reduced. By adjusting the installation position of the classifying element even in a low case, the air flow velocity distribution in the radial direction of the pipeline and the pulverized coal concentration distribution can be adjusted to an optimum state by providing a pulverized coal supply device. Achieved.

本発明の構成は、特許請求の範囲の請求項1に記載の
ように、 微粉炭を空気で搬送して微粉炭バーナへ供給して燃焼
させる管路を有する微粉炭燃焼装置において、上記管路
の微粉炭放出端に対して前流側から、分級エレメント
と、案内筒を設け、上記管路の半径方向の微粉炭濃度分
布を管路の微粉炭放出端まで維持すると共に、管路の半
径方向の空気流速分布を管路の微粉炭放出端でほぼ一定
になるように、上記分級エレメントは、管路の中心軸方
向に自在に設置位置の調整が可能な構造に設けた微粉炭
燃焼装置とするものである。
According to a first aspect of the present invention, there is provided a pulverized coal combustion apparatus having a pipe for conveying pulverized coal by air, supplying the pulverized coal to a pulverized coal burner, and burning the pulverized coal. From the upstream side of the pulverized coal discharge end, a classification element and a guide cylinder are provided to maintain the pulverized coal concentration distribution in the radial direction of the pipe up to the pulverized coal discharge end of the pipe, and the radius of the pipe Coal pulverized combustion device provided with a structure in which the installation position can be freely adjusted in the direction of the central axis of the pipeline so that the air velocity distribution in the direction is substantially constant at the pulverized coal discharge end of the pipeline. It is assumed that.

また、本発明は請求項2に記載のように、請求項1の
微粉炭燃焼装置において、微粉炭の分級エレメントは、
微粉炭供給管路の中心軸方向に設けられた支持体上を、
スライドレバー機構により上記分級エレメントをスライ
ドさせて、該分級エレメントの設置位置を自在に調整可
能な構造にした微粉炭燃焼装置とするものである。
Further, according to the present invention, as described in claim 2, in the pulverized coal combustion device of claim 1, the pulverized coal classification element includes:
On the support provided in the center axis direction of the pulverized coal supply pipeline,
The pulverized coal combustion device has a structure in which the classification element is slid by a slide lever mechanism so that the installation position of the classification element can be freely adjusted.

〔作用〕[Action]

微粉炭濃度が低い場合であっても微粉炭の分級エレメ
ントの設置位置を自在に調整することにより、空気流速
分布が均一で微粉炭濃度の高められた混合気を保炎リン
グ近傍に供給することができる。これによって、保炎リ
ング近傍で着火に必要な微粉炭濃度を確保することがで
き、安定した微粉炭火炎が得られる。
Even if the pulverized coal concentration is low, the airflow distribution is uniform and the mixture with an increased pulverized coal concentration is supplied to the vicinity of the flame holding ring by freely adjusting the installation position of the pulverized coal classification element. Can be. As a result, the concentration of pulverized coal required for ignition in the vicinity of the flame holding ring can be secured, and a stable pulverized coal flame can be obtained.

〔実施例〕〔Example〕

以下に本発明の一実施例を挙げ、図面に基づいて、さ
らに詳細に説明する。
Hereinafter, an embodiment of the present invention will be described in more detail with reference to the drawings.

第1図は本発明の微粉炭供給装置を適用した微粉炭バ
ーナの構成の一例を示す断面図である。図において、1
次空気と共に微粉炭供給管内を搬送されてきた微粉炭流
12は、バーナの1次空気スリーブ11内の中心部のディス
タンスピース8に設けたブロック状の微粉炭の分級エレ
メント10に衝突した1次空気および微粉炭は1次空気ス
リーブ11の内壁に沿った流れとなり、分級エレメント10
の後流側の滑らかなテーパにより1次空気流速は断面方
向に均一に回復されるが、この1次空気流に比べ大きな
運動量を持った微粉炭は、内壁に沿った流れを維持する
ことにより、1次空気スリーブ11の内壁側の微粉炭濃度
を高くすることができる。
FIG. 1 is a sectional view showing an example of the configuration of a pulverized coal burner to which the pulverized coal supply device of the present invention is applied. In the figure, 1
Pulverized coal flow conveyed in the pulverized coal supply pipe with secondary air
Reference numeral 12 denotes primary air and pulverized coal that collided with the block-shaped pulverized coal classification element 10 provided on the distance piece 8 at the center in the primary air sleeve 11 of the burner along the inner wall of the primary air sleeve 11. It becomes a flow and the classification element 10
The primary air flow velocity is recovered uniformly in the cross-sectional direction by the smooth taper on the downstream side of the pulverized coal. However, the pulverized coal having a larger momentum than this primary air flow is maintained by maintaining the flow along the inner wall. First, the pulverized coal concentration on the inner wall side of the primary air sleeve 11 can be increased.

しかし、そのままでは1次空気スリーブ11の微粉炭放
出端に取付けた保炎リング6に到達する前に、微粉炭濃
度分布は均一化され、保炎リング6近傍に高濃度の微粉
炭を供給することができなくなるので、分級エレメント
10の後流にできた理想的な濃度分布(空気流速が均一、
微粉炭濃度は中心部が低く管壁部が高い)を、そのまま
保炎リング6の位置まで維持するために案内筒7を設け
ている。これにより、保炎リング6近傍の微粉炭濃度が
高くなり、微粉炭への初期着火性が向上し、安定した保
炎が可能となる。
However, as it is, before reaching the flame holding ring 6 attached to the pulverized coal discharging end of the primary air sleeve 11, the pulverized coal concentration distribution is made uniform, and high concentration pulverized coal is supplied near the flame holding ring 6. Classifying element
10 Ideal concentration distribution in the wake (air velocity is uniform,
A guide cylinder 7 is provided to maintain the pulverized coal concentration at the center and low at the center of the pipe wall) to the position of the flame holding ring 6 as it is. Thereby, the pulverized coal concentration in the vicinity of the flame holding ring 6 is increased, the initial ignitability of the pulverized coal is improved, and stable flame holding becomes possible.

また、分級エレメント10はディスタンスピース8上を
スライドできる構造となっており、このスライドさせて
分級エレメント10の設置位置調整による効果を、第2
図、第3図および第4図に示す。
Further, the classifying element 10 has a structure that can slide on the distance piece 8.
This is shown in FIGS. 3, 3 and 4.

第2図は、分級エレメント10と案内筒7との距離を大
きくした場合で、この場合には、分級エレメント10の後
流側の微粉炭濃度分布および空気流速分布は均一化され
て本発明の効果は生じない。逆に、第4図に示すよう
に、案内筒7に分級エレメント10を近づけ過ぎた場合に
は、微粉炭濃度分布だけをとってみると理想的な濃度分
布になるが、空気流速分布は、1次空気スリーブ11の内
壁側が速くなり、保炎リング6の後流側に発生する着火
に必要な微小渦の生成を邪魔することになり、その結果
保炎性は低下する。
FIG. 2 shows a case where the distance between the classification element 10 and the guide cylinder 7 is increased. In this case, the pulverized coal concentration distribution and the air velocity distribution on the downstream side of the classification element 10 are made uniform, and No effect. Conversely, as shown in FIG. 4, when the classification element 10 is brought too close to the guide cylinder 7, an ideal concentration distribution is obtained when only the pulverized coal concentration distribution is taken, but the air flow velocity distribution is as follows. The inner wall side of the primary air sleeve 11 becomes faster, hindering the generation of minute vortices necessary for ignition generated on the downstream side of the flame holding ring 6, and as a result, the flame holding property is reduced.

つまり、分級エレメント10と案内筒7の位置関係を最
適な位置に調整することにより、低負荷時に微粉炭濃度
が低くなっても、第3図に示すごとく理想的な微粉炭濃
度分布と空気流速分布を得ることができる。
That is, by adjusting the positional relationship between the classifying element 10 and the guide cylinder 7 to an optimum position, even if the pulverized coal concentration becomes low at a low load, as shown in FIG. A distribution can be obtained.

上記の実施例においては、1次空気スリーブ11の先端
部に保炎リング6を有する微粉炭バーナについて述べた
が、本実施例の効果は保炎リングを設けない微粉炭バー
ナにおいても適用できる。
In the above embodiment, the pulverized coal burner having the flame holding ring 6 at the end of the primary air sleeve 11 has been described. However, the effect of this embodiment can be applied to a pulverized coal burner without a flame holding ring.

〔発明の効果〕〔The invention's effect〕

以上詳細に説明したごとく、本発明の微粉炭燃焼装置
を設けた微粉炭バーナは、微粉炭供給管路に、微粉炭の
分級エレメントと空気流の案内筒を設け、かつ微粉炭の
分級エレメントの位置を調整することにより、微粉炭の
放出端における微粉炭濃度分布と空気流速分布とを最適
に制御することができ、次に示す効果が得られる。
As described in detail above, the pulverized coal burner provided with the pulverized coal combustion device of the present invention is provided with a pulverized coal classification element and an air flow guide cylinder in the pulverized coal supply line, and a pulverized coal classification element. By adjusting the position, the pulverized coal concentration distribution and the air flow velocity distribution at the discharge end of the pulverized coal can be optimally controlled, and the following effects can be obtained.

(1)微粉炭バーナへの新しい機能の付加として、微粉
炭放出端における微粉炭濃度分布を調整することによる
着火、保炎性が向上する。
(1) As a new function added to the pulverized coal burner, the ignition and flame holding properties are improved by adjusting the pulverized coal concentration distribution at the pulverized coal discharge end.

(2)微粉炭バーナの性能、効率の向上として、バーナ
の低負荷燃焼時における火炎の安定化をはかることがで
きる。
(2) As an improvement in the performance and efficiency of the pulverized coal burner, it is possible to stabilize the flame during low load combustion of the burner.

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

第1図は本発明の実施例において例示した微粉炭バーナ
の側断面図、第2図、第3図および第4図は第1図の微
粉炭バーナの微粉炭供給管路の分級エレメントの位置を
変化させた時の微粉炭放出端における微粉炭濃度分布と
空気流速分布を示す模式図、第5図は従来の微粉炭バー
ナの微粉炭供給管路の構成と微粉炭放出端における微粉
炭濃度分布と空気流速分布を示す模式図である。 1……風箱、2……2次空気レジスタ 3……3次空気レジスタ、4……バーナスロート 5……2次空気ベーン、6……保炎リング 7……案内筒、8……ディスタンスピース 9……スライドレバー、10……分級エレメント 11……1次空気スリーブ 12……微粉炭流、13……微粉炭(高濃度) 14……微粉炭(低濃度) 15……ベンチュリ、16……点火用トーチ
FIG. 1 is a side sectional view of a pulverized coal burner exemplified in an embodiment of the present invention, and FIGS. 2, 3 and 4 show positions of a classification element of a pulverized coal supply line of the pulverized coal burner of FIG. Fig. 5 is a schematic diagram showing a pulverized coal concentration distribution and an air flow velocity distribution at a pulverized coal discharge end when the air temperature is changed. It is a schematic diagram which shows a distribution and an air flow velocity distribution. 1 ... wind box, 2 ... secondary air register 3 ... tertiary air register 4, ... burner throat 5 ... secondary air vane, 6 ... flame holding ring 7 ... guide cylinder, 8 ... distance Piece 9: Slide lever, 10: Classifying element 11: Primary air sleeve 12: Pulverized coal flow, 13: Pulverized coal (high concentration) 14: Pulverized coal (low concentration) 15: Venturi, 16 ...... Ignition torch

フロントページの続き (72)発明者 神保 正 広島県呉市宝町6番9号 バブコック日 立株式会社呉工場内 (56)参考文献 実開 平1−136218(JP,U) (58)調査した分野(Int.Cl.6,DB名) F23D 1/00Continuation of the front page (72) Inventor Tadashi Jimbo 6-9 Takara-cho, Kure City, Hiroshima Prefecture Inside the Kure Factory of Babcock Hitachi, Ltd. (56) References Bikai 1-136218 (JP, U) (58) Fields surveyed (Int.Cl. 6 , DB name) F23D 1/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】微粉炭を空気で搬送して微粉炭バーナへ供
給して燃焼させる管路を有する微粉炭燃焼装置におい
て、上記管路の微粉炭放出端に対して前流側から分級エ
レメントと案内筒を設け、上記分級エレメントは管路の
半径方向の微粉炭濃度分布を調整可能な構造に設け、上
記案内筒は上記分級エレメントによる管路の半径方向の
微粉炭濃度分布を上記管路の微粉炭放出端まで維持する
ように設けたことを特徴とする微粉炭燃焼装置。
1. A pulverized coal combustion apparatus having a pipe for conveying pulverized coal by air, supplying the pulverized coal to a pulverized coal burner, and burning the pulverized coal. A guide cylinder is provided, and the classification element is provided in a structure capable of adjusting the pulverized coal concentration distribution in the radial direction of the pipeline, and the guide cylinder is configured to adjust the pulverized coal concentration distribution in the radial direction of the pipeline by the classification element of the pipeline. A pulverized coal combustion apparatus characterized in that it is provided so as to maintain the pulverized coal discharge end.
【請求項2】請求項1に記載の微粉炭燃焼装置におい
て、上記分級エレメントは管路内を空気および微粉炭の
流れ方向に自在に設置位置の調整が可能な構造に設けた
ことを特徴とする微粉炭燃焼装置。
2. The pulverized coal combustion apparatus according to claim 1, wherein the classifying element is provided in a structure in which the installation position can be freely adjusted in the flow direction of air and pulverized coal in the pipeline. Pulverized coal combustion equipment.
JP1246400A 1989-09-25 1989-09-25 Pulverized coal combustion equipment Expired - Fee Related JP2781222B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1246400A JP2781222B2 (en) 1989-09-25 1989-09-25 Pulverized coal combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1246400A JP2781222B2 (en) 1989-09-25 1989-09-25 Pulverized coal combustion equipment

Publications (2)

Publication Number Publication Date
JPH03110308A JPH03110308A (en) 1991-05-10
JP2781222B2 true JP2781222B2 (en) 1998-07-30

Family

ID=17147949

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1246400A Expired - Fee Related JP2781222B2 (en) 1989-09-25 1989-09-25 Pulverized coal combustion equipment

Country Status (1)

Country Link
JP (1) JP2781222B2 (en)

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CN102080822B (en) * 2010-12-22 2013-03-27 阿米那能源环保技术(中国)有限公司 Combustor and manufacturing method thereof
JP2013178040A (en) * 2012-02-28 2013-09-09 Mitsubishi Heavy Ind Ltd Pulverized coal supply pipe

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