JP2738705B2 - Pulverized coal burner and pulverized coal combustion device using it - Google Patents

Pulverized coal burner and pulverized coal combustion device using it

Info

Publication number
JP2738705B2
JP2738705B2 JP63173939A JP17393988A JP2738705B2 JP 2738705 B2 JP2738705 B2 JP 2738705B2 JP 63173939 A JP63173939 A JP 63173939A JP 17393988 A JP17393988 A JP 17393988A JP 2738705 B2 JP2738705 B2 JP 2738705B2
Authority
JP
Japan
Prior art keywords
pulverized coal
burner
coal
fine
particles
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
JP63173939A
Other languages
Japanese (ja)
Other versions
JPH0225609A (en
Inventor
公哉 坂本
忠久 政井
文夫 幸田
茂樹 森田
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi 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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP63173939A priority Critical patent/JP2738705B2/en
Publication of JPH0225609A publication Critical patent/JPH0225609A/en
Application granted granted Critical
Publication of JP2738705B2 publication Critical patent/JP2738705B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は微粉炭の燃焼装置に係り、特に高燃料比炭
(低揮発分炭)の微粉炭燃焼において、保炎性が極めて
良好で、火炎安定燃焼範囲の大きいバーナ装置およびそ
れを用いた微粉炭燃焼装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a pulverized coal combustion apparatus, and particularly in the case of pulverized coal combustion of high fuel ratio coal (low volatile coal), it has extremely good flame holding properties. The present invention relates to a burner device having a large flame stable combustion range and a pulverized coal combustion device using the burner device.

〔従来の技術〕[Conventional technology]

従来の微粉炭燃焼装置は、例えば第4図に示すごと
く、微粉炭輸送管2の途中に、サイクロン型の微粉炭濃
度上昇器3を装備しているものの、排気管5は直接微粉
炭バーナ13に接続されていて、排気管5内の気流中に含
まれている微細な石炭の微粒子を回収する配慮は全くな
されていなかった。〔火力原子力発電第38巻第367号
(昭和62年4月号)第61頁〕。また、排気管5内の微細
石炭粒子の量は、排気管5内の空気量に対して極めて僅
かな量であるため、それ自体で微粉炭火炎を形成させる
ことが不可能であり、したがって、微粉炭バーナの保炎
機能向上を寄与するように利用することなど全く考えら
れていなかった。
The conventional pulverized coal combustion apparatus is equipped with a cyclone type pulverized coal concentration riser 3 in the middle of the pulverized coal transport pipe 2 as shown in FIG. 4, for example, but the exhaust pipe 5 is directly connected to the pulverized coal burner 13. And no consideration has been given to recovering fine coal particles contained in the airflow in the exhaust pipe 5. [Thermal and Nuclear Power, Vol. 38, No. 367 (April 1987), page 61]. Further, since the amount of the fine coal particles in the exhaust pipe 5 is extremely small with respect to the amount of air in the exhaust pipe 5, it is impossible to form a pulverized coal flame by itself, and therefore, The use of pulverized coal burners to improve the flame holding function was never considered.

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

微粉炭バーナ、特に高燃料比炭を燃焼させる微粉炭バ
ーナにおいて、バーナの保炎性能に影響を及ぼす主な要
因は、 (1)微粉炭と搬送空気の割合、すなわち搬送空気中の
微粉炭濃度, (2)搬送空気の温度, (3)微粉炭の粒度, などが挙げられる。
In a pulverized coal burner, particularly in a pulverized coal burner burning high-fuel-ratio coal, the main factors affecting the flame holding performance of the burner are: (1) The ratio of pulverized coal to carrier air, that is, the concentration of pulverized coal in the carrier air. , (2) the temperature of the carrier air, (3) the particle size of the pulverized coal, and the like.

上記要因の(1)については、微粉炭濃度〔石炭(k
g)/空気(kg)〕が大きい程バーナの保炎性が良く、
(2)については、搬送空気の温度が高い程バーナの保
炎性が良好となり、さらに(3)については、微粉炭の
粒径が約30μm以下の微粒子が多い程、バーナの保炎性
能は向上する。
Regarding the above factor (1), the pulverized coal concentration [coal (k
g) / air (kg)], the better the flame holding properties of the burner.
Regarding (2), the higher the temperature of the conveying air, the better the flame holding properties of the burner. Regarding (3), the more the fine particles having a particle size of pulverized coal of about 30 μm or less, the better the flame holding performance of the burner. improves.

しかしながら、実際に微粉炭バーナと連結して運転さ
れる石炭粉砕ミルの制御機能上の問題から、上記(1)
および(2)の要因には、おのずからその上限が存在し
ており、しかも、微粉炭濃度をあまり大きくせず、また
搬送空気の温度をあまり高くしない方が微粉炭バーナの
運転上好都合である。また、上記(3)の要因について
は、石炭粉砕ミルの粉砕能力と微粉炭輸送管2の途中に
設置される微粉炭濃度上昇器3の微粒子の捕集性能によ
って支配され、従来の微粉炭バーナでは、微粉炭の粒度
をバーナの保炎上望ましい値の範囲に調整することがで
きないという問題があった。
However, due to the problem of the control function of the coal pulverizing mill actually operated in connection with the pulverized coal burner, the above (1)
Factors (2) naturally have their upper limits, and it is more convenient to operate the pulverized coal burner if the pulverized coal concentration is not too high and the temperature of the conveying air is not too high. The factor (3) is governed by the pulverizing capacity of the coal pulverizing mill and the collecting performance of the fine particles of the pulverized coal concentration increasing device 3 installed in the middle of the pulverized coal transport pipe 2. Thus, there was a problem that the particle size of the pulverized coal could not be adjusted to a value within a desirable range for the flame holding of the burner.

本発明の目的は、上記従来技術の問題点を解消し、微
粉炭バーナの保炎性能を向上させるのに最適な微粉炭粒
度に保持して、高燃料比炭の火炎安定燃焼範囲の拡大を
はかる微粉炭バーナおよびそれを用いた微粉炭燃焼装置
を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art, and to maintain the pulverized coal particle size optimal for improving the flame holding performance of the pulverized coal burner to expand the flame stable combustion range of high fuel ratio coal. An object of the present invention is to provide a pulverized coal burner to be measured and a pulverized coal combustion device using the burner.

〔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、微粉炭燃焼バーナ装置におい
て、微粉炭輸送管路に設けられている微粉炭濃度上昇器
から排気される微細石炭粒子(粒径が約30μm以下のも
の)を捕集し回収する、例えばバグフィルタ式の捕集器
を配置し、該捕集器によって捕集された微細石炭粒子
を、該微細石炭粒子の誘導板を設けた微粉炭バーナのバ
ーナ筒の内部に注入し、燃焼させることにより、達成さ
れる。
An object of the present invention is to provide a pulverized coal combustion burner device which collects fine coal particles (having a particle size of about 30 μm or less) exhausted from a pulverized coal concentration riser provided in a pulverized coal transportation pipeline. For example, a collector of a bag filter type is disposed for collection, and the fine coal particles collected by the collector are injected into a burner cylinder of a pulverized coal burner provided with a guide plate for the fine coal particles. Is achieved by burning.

本発明の微粉炭バーナは、バーナスロート内に、燃焼
用空気を供給する3次空気レジスタとガイドスリーブ、
2次空気レジスタと2次空気ベーンおよび微粉炭輸送管
路から気流輸送される微粉炭と空気の混合気流を、燃焼
炉内へ供給するバーナ筒を少なくとも備え、かつ上記バ
ーナ筒の炉内側先端部に保炎器を設けた微粉炭バーナで
あって、上記バーナ筒の炉外側の一端に、微粉炭供給系
において捕集された微細石炭粒子を、上記バーナ筒の内
部に注入する注入器を設けた微粉炭バーナである。
The pulverized coal burner according to the present invention includes a tertiary air register and a guide sleeve for supplying combustion air into a burner throat.
A burner tube for supplying a mixed air flow of pulverized coal and air pneumatically transported from a secondary air register, a secondary air vane, and a pulverized coal transport line into a combustion furnace, and a tip end inside the furnace of the burner tube; Pulverized coal burner provided with a flame stabilizer, provided at one end of the furnace outside the burner cylinder, an injector for injecting the fine coal particles collected in the pulverized coal supply system into the interior of the burner cylinder. Pulverized coal burner.

そして、本発明の微粉炭バーナにおいて、バーナ筒の
内部に、該バーナ筒の内面との間に所定の空間を形成す
る微細石炭粒子の誘導板を設けることが好ましい。さら
に、本発明の微粉炭バーナにおいて、バーナ筒の内部に
設置した微細石炭粒子の誘導板の炉外側先端部に、ベル
マウス型の案内板を設けることが望ましい。
And in the pulverized coal burner of the present invention, it is preferable to provide a guide plate of fine coal particles which forms a predetermined space between the burner cylinder and the inner surface of the burner cylinder. Further, in the pulverized coal burner of the present invention, it is desirable to provide a bellmouth type guide plate at the furnace outer end of the guide plate of fine coal particles installed inside the burner cylinder.

本発明の微粉炭燃焼装置は、微粉炭を供給する石炭粉
砕ミルと、該ミルによって生成した微粉炭を、微粉炭輸
送管路に設置されている微粉炭濃度上昇器を経由して、
本発明の微粉炭バーナに供給し燃焼させる微粉炭燃焼装
置であって、上記微粉炭濃度上昇器の排気管から排出さ
れる微細石炭粒子を捕集する、例えばバグフイルタ式の
捕集器を設置し、該捕集器によって捕集された微細石炭
粒子を、上記微粉炭バーナのバーナ筒に設けられている
微細石炭粒子の注入器に連結する管路を配設したもので
ある。
The pulverized coal combustion device of the present invention, a coal pulverizing mill for supplying pulverized coal, and pulverized coal generated by the mill, via a pulverized coal concentration riser installed in a pulverized coal transport pipeline,
A pulverized coal combustion device for supplying and burning a pulverized coal burner according to the present invention, wherein a pulverized coal burner for collecting fine coal particles discharged from an exhaust pipe of the pulverized coal concentration raiser, for example, a bag filter type collector is provided. And a conduit for connecting the fine coal particles collected by the collector to a fine coal particle injector provided in a burner cylinder of the pulverized coal burner.

また、本発明の微粉炭燃焼装置において、捕集器によ
って捕集された微細石炭粒子を、微粉炭バーナに微粉炭
を供給する微粉炭輸送管に注入する管路を配設しても、
本発明の目的は達成される。
Further, in the pulverized coal combustion device of the present invention, even if a conduit for injecting the fine coal particles collected by the collector into the pulverized coal transport pipe for supplying pulverized coal to the pulverized coal burner is provided,
The object of the present invention is achieved.

〔作用〕 微粉炭濃度上昇器としては、通常の場合、サイクロン
のような機械式の微粉炭濃度上昇器が用いられるため、
バーナの保炎上望ましい約30μm以下の微細石炭粒子
が、微粉炭濃度上昇器の排気管から排出されるため、微
粉炭輸送管を経由して微粉炭バーナのバーナ筒に至る微
粉炭と空気の混合気流中に含まれる保炎上望ましい微細
石炭粒子の割合が極端に減少することになる。しかし、
本発明による微粉炭燃焼手段を用いることによって、い
ったん逸失した微細石炭粒子を捕集し回収して、微粉炭
バーナのバーナ筒部またはバーナに至る微粉炭輸送管路
内に注入する結果、微粉炭バーナによって保炎上望まし
い石炭の微粒子粒度に保持することができるので、バー
ナの火炎安定燃焼範囲を拡大することができ、高燃料比
炭でも安定した微粉炭燃焼を継続させることが可能とな
る。
[Action] As a pulverized coal concentration increaser, a mechanical pulverized coal concentration increaser such as a cyclone is usually used.
Mixing of pulverized coal and air that reaches the burner cylinder of the pulverized coal burner via the pulverized coal transport pipe because fine coal particles of about 30μm or less, which are desirable for flame holding of the burner, are discharged from the exhaust pipe of the pulverized coal concentration riser. The proportion of fine coal particles desired for flame holding contained in the air stream will be extremely reduced. But,
By using the pulverized coal combustion means according to the present invention, the fine coal particles once lost are collected and collected, and injected into the burner cylinder of the pulverized coal burner or into the pulverized coal transportation pipeline leading to the burner. Since the burner can maintain the desired fine particle size of coal for flame holding, the flame stable combustion range of the burner can be expanded, and stable pulverized coal combustion can be continued even with high fuel ratio coal.

また、バーナ筒の微細石炭粒子の注入部には誘導板を
設置して、微細石炭粒子が、いたずらに微粉炭と空気の
混合気流中に拡散されるのを防止し、バーナノズル先端
部の保炎部分に効率よく微細石炭粒子が誘導されるよう
に機能している。
In addition, a guide plate is installed at the injection part of the fine coal particles in the burner cylinder to prevent the fine coal particles from being unnecessarily diffused into the mixed air flow of pulverized coal and air, and the flame holding at the tip of the burner nozzle. It functions so that fine coal particles are efficiently guided to the part.

〔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、本発明の微粉炭バーナの断面構造を示す模
式図であって、バーナ本体は、バーナスロート11、ガイ
ドスリーブ12、2次空気レジスタ14、3次空気レジスタ
15、2次空気ベーン16およびバーナ筒10によって構成さ
れている。バーナ筒10の炉内側先端部には保炎器17を備
え、この保炎器17によって巻き込まれた2次空気は保炎
器の内側で微小渦を形成するので、バーナ筒10から炉内
側に噴出された微粉炭はこの付近で着火する。2次空気
レジスタ14、3次空気レジスタ15および2次空気ベーン
16は旋回器として機能し、低NOx燃焼など、目的に応じ
た火炎構造を形成するように調整される。
FIG. 1 is a schematic view showing a cross-sectional structure of a pulverized coal burner of the present invention, in which a burner body includes a burner throat 11, a guide sleeve 12, a secondary air register 14, and a tertiary air register.
15, a secondary air vane 16 and a burner cylinder 10. A burner 17 is provided at the front end of the burner tube 10 inside the furnace, and the secondary air entrained by the burner 17 forms a small vortex inside the flame holder. The pulverized coal ignited near here. Secondary air register 14, Tertiary air register 15 and Secondary air vane
16 functions as a swirler and is adjusted to form a flame structure according to the purpose, such as low NOx combustion.

バーナ筒10の外側に取り付けられた注入器9は、それ
を通じてバーナ筒10内に微細石炭粒子を送入するための
もので、バーナ筒10の内側には、ちようど微細石炭粒子
をバーナ筒10の内面に沿わせて、炉内側先端部の保炎器
17近傍にまで導くための誘導板18が装着されている。バ
ーナ筒10の内面と誘導板18の外面との間に形成される空
間には、上記の微細石炭粒子が適切な速度で炉内側先端
部の保炎器17の近傍にまで搬送されるように、微粉炭輸
送管4から流入してくる空気の一部が取り込まれるよう
にする。ベルマウス型の案内板19は、空気の取り込みを
容易にすると共に、適正な空気量が配分されるように、
その形状が設定されている。
The injector 9 mounted on the outside of the burner tube 10 is for feeding fine coal particles into the burner tube 10 therethrough. Inside the burner tube 10, fine coal particles are injected into the burner tube 10. Along the inner surface of 10, the flame stabilizer at the tip inside the furnace
A guide plate 18 for leading to the vicinity of 17 is mounted. In the space formed between the inner surface of the burner cylinder 10 and the outer surface of the guide plate 18, the fine coal particles are conveyed at an appropriate speed to the vicinity of the flame stabilizer 17 at the front end of the furnace. A part of the air flowing from the pulverized coal transport pipe 4 is taken in. The bellmouth type guide plate 19 facilitates the intake of air and distributes the appropriate amount of air.
Its shape is set.

第2図は、石炭粉砕ミル1から連結されている微粉炭
輸送管2の途中に設置されたサイクロン型の微粉炭濃度
上昇器3からの排気管5中の微細石炭粒子を、バグフィ
ルタ型の微細石炭粒子捕集器6で回収すると共に、空気
のみを排気管8から大気中へ放出させる。一方、微細石
炭粒子は、空気流または機械的搬送手段によって、微細
石炭粒子輸送管7よりバーナ筒10の注入部9からバーナ
筒10の内部へ導入する構成例を示すものである。
FIG. 2 shows the fine coal particles in the exhaust pipe 5 from the cyclone type pulverized coal concentration riser 3 installed in the middle of the pulverized coal transport pipe 2 connected to the coal pulverizing mill 1, and the bag filter type. While being collected by the fine coal particle collector 6, only air is discharged from the exhaust pipe 8 to the atmosphere. On the other hand, a configuration example is shown in which the fine coal particles are introduced into the burner cylinder 10 from the injection portion 9 of the burner cylinder 10 from the fine coal particle transport pipe 7 by an air flow or a mechanical conveying means.

バーナ筒10の内面と誘導板18の外面とによって形成さ
れる環状の空隙部内を、炉内側先端部に向けて搬送され
た微細石炭粒子は、保炎器17近傍に至ると、2次空気の
巻み込みによって、保炎器17の後流に形成される微小空
気渦の流れに伴流して、バーナの着火保持上肝要な燃料
源として有効に機能することになる。
The fine coal particles conveyed toward the furnace inner end portion in the annular space formed by the inner surface of the burner cylinder 10 and the outer surface of the guide plate 18 reach the vicinity of the flame stabilizer 17 and form secondary air. The entrainment causes the flow of the minute air vortex formed behind the flame stabilizer 17 to effectively function as a fuel source essential for maintaining the burner ignition.

〔発明の効果〕〔The invention's effect〕

以上詳細に説明したごとく、本発明の微粉炭バーナお
よびそれを用いた微粉炭燃焼装置によれば以下に示す効
果がある。
As described above in detail, the pulverized coal burner of the present invention and the pulverized coal combustion apparatus using the same have the following effects.

(1)バーナの火炎安定に大きく寄与する微細石炭粒子
(約30μm以下)を、微細石炭粒子の濃度を小さくする
ことなくバーナの保炎器部に供給することができるの
で、火炎燃焼範囲を拡大することができ安定した微粉炭
燃焼を継続させることができる。
(1) Fine coal particles (approximately 30 μm or less) that greatly contribute to the flame stability of the burner can be supplied to the flame stabilizer of the burner without reducing the concentration of the fine coal particles, thereby expanding the flame combustion range. And stable pulverized coal combustion can be continued.

(2)保炎上有効な微細石炭粒子を回収して、適正な微
細石炭粒子濃度に調整してバーナに供給することができ
るので、第3図に示すように、無煙炭、低質炭のような
高燃料比炭の火炎安定燃焼範囲を拡大することが可能と
なる。
(2) Since fine coal particles effective for flame holding can be recovered and adjusted to an appropriate fine coal particle concentration and supplied to a burner, as shown in FIG. It is possible to expand the flame stable combustion range of the fuel-to-fuel ratio.

(3)ボイラのスタートアップ時のようなバーナ負荷の
低い燃焼条件(2次,3次空気温度が低く、微粉炭/搬送
空気の重量比が小さく、火炎が極めて不安定)下での助
燃用油の使用量の低減をはかることができる。
(3) Fuel oil for combustion under low burner load conditions such as boiler start-up (low secondary and tertiary air temperatures, low pulverized coal / transport air weight ratio, extremely unstable flame) Can be reduced.

【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
の断面構造を示す模式図、第2図は本発明の微粉炭バー
ナを微粉炭燃焼システムに適用した場合の系統図、第3
図は実施例において例示した本発明の微粉炭バーナの火
炎安定範囲を示すグラフ、第4図は従来の微粉炭燃焼シ
ステムを示す系統図である。 1……石炭粉砕ミル、2……微粉炭輸送管 3……微粉炭濃度上昇器 4……微粉炭輸送管、5……排気管 6……微細石炭粒子捕集器 7……微細石炭粒子輸送管 8……排気管、9……注入器 10……バーナ筒、11……バーナスロート 12……ガイドスリーブ、14……2次空気レジスタ 15……3次空気レジスタ、16……2次空気ベーン 17……保炎器、18……誘導板 19……案内板
FIG. 1 is a schematic view showing a sectional structure of a pulverized coal burner exemplified in the embodiment of the present invention, FIG. 2 is a system diagram in a case where the pulverized coal burner of the present invention is applied to a pulverized coal combustion system, and FIG.
FIG. 4 is a graph showing a flame stable range of the pulverized coal burner of the present invention exemplified in the embodiment, and FIG. 4 is a system diagram showing a conventional pulverized coal combustion system. DESCRIPTION OF SYMBOLS 1 ... Coal pulverizing mill, 2 ... Pulverized coal transportation pipe 3 ... Pulverized coal concentration raiser 4 ... Pulverized coal transportation pipe 5, ... Exhaust pipe 6 ... Fine coal particle collector 7 ... Fine coal particles Transport pipe 8 ... Exhaust pipe, 9 ... Injector 10 ... Burner cylinder, 11 ... Burner throat 12 ... Guide sleeve, 14 ... Secondary air register 15 ... Tertiary air register, 16 ... Secondary Air vane 17 …… flame holder, 18 …… guide plate 19 …… guide plate

───────────────────────────────────────────────────── フロントページの続き (72)発明者 森田 茂樹 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 特開 昭57−12209(JP,A) 特開 昭62−116810(JP,A) 特開 平1−117444(JP,A) 特開 昭60−223914(JP,A) 特開 昭61−44214(JP,A) 特開 昭62−210308(JP,A) ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Shigeki Morita 6-9 Takara-cho, Kure-shi, Hiroshima Pref. Inside the Kure Plant of Babcock Hitachi Ltd. (56) References JP-A-57-12209 (JP, A) JP-A Sho 62-116810 (JP, A) JP-A-1-117444 (JP, A) JP-A-60-223914 (JP, A) JP-A-61-44214 (JP, A) JP-A-62-210308 (JP, A) A)

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】バーナスロート内に、石炭粉砕ミルからの
微粉炭輸送管路により気流輸送される微粉炭と空気の混
合気流を燃焼炉内へ供給するバーナ筒と、該バーナ筒の
外側に燃焼用空気を燃焼炉内へ供給する流路とを備え、
上記バーナ筒の炉内側先端部に保炎器を設けた微粉炭バ
ーナにおいて、上記微粉炭輸送管路の途中に、上記バー
ナ筒への微粉炭濃度を調節する機械式の微粉炭濃度調節
手段と、該微粉炭濃度調節手段からの排気管路に、排気
中に含まれる微細な石炭粒子を回収する微細石炭粒子捕
集手段と、上記バーナ筒の外側に、上記微細石炭粒子捕
集手段により捕集した微細石炭粒子が、バータ筒を流れ
る混合気流によって、バーナ筒の内面に沿って、上記保
炎器近傍に搬送されるように、微細石炭粒子をバーナ筒
の内部へ注入する手段を設けたことを特徴とする微粉炭
バーナ。
1. A burner cylinder for supplying a mixed air flow of pulverized coal and air, which is pneumatically transported by a pulverized coal transportation pipe from a coal pulverizing mill, into a burner throat, and burns outside the burner cylinder. A flow path for supplying working air into the combustion furnace,
In a pulverized coal burner provided with a flame stabilizer at the furnace inner end of the burner cylinder, in the middle of the pulverized coal transport pipeline, a mechanical pulverized coal concentration adjusting means for adjusting the pulverized coal concentration to the burner cylinder. A fine coal particle collecting means for collecting fine coal particles contained in exhaust gas in an exhaust pipe from the fine coal concentration controlling means, and a fine coal particle collecting means outside the burner cylinder. Means are provided for injecting the fine coal particles into the burner tube so that the collected fine coal particles are conveyed to the vicinity of the flame stabilizer along the inner surface of the burner tube by the mixed gas flow flowing through the burner tube. A pulverized coal burner, characterized in that:
【請求項2】請求項1記載の微粉炭バーナにおいて、バ
ーナ筒の内部に、該バーナ筒の内面と所定の空間を形成
する微細石炭粒子の誘導板を設けたことを特徴とする微
粉炭バーナ。
2. A pulverized coal burner according to claim 1, wherein a guide plate of fine coal particles forming a predetermined space with the inner surface of the burner cylinder is provided inside the burner cylinder. .
【請求項3】請求項1または請求項2記載の微粉炭バー
ナにおいて、バーナ筒の内部に設置した微細石炭粒子の
誘導板の炉外側先端部に、ベルマウス型の案内板を設け
たことを特徴とする微粉炭バーナ。
3. A pulverized coal burner according to claim 1 or 2, wherein a bellmouth type guide plate is provided at a front end portion of the induction plate of the fine coal particles installed inside the burner cylinder on the outside of the furnace. Characterized pulverized coal burner.
【請求項4】微粉炭を供給する石炭粉砕ミルと、該ミル
によって生成した微粉炭を、微粉炭輸送管路に設置され
ている微粉炭濃度上昇器を経由して、請求項1に記載の
微粉炭バーナに供給し燃焼させる微粉炭燃焼装置におい
て、上記微粉炭濃度上昇器の排気管から排出される微細
石炭粒子を捕集する捕集器を設置し、該捕集器によって
捕集された微細石炭粒子を、上記微粉炭バーナのバーナ
筒に設けられている微細石炭粒子の注入器に連結する管
路を配設したことを特徴とする微粉炭燃焼装置。
4. The coal pulverizing mill for supplying pulverized coal, and the pulverized coal produced by the mill are passed through a pulverized coal concentration raiser installed in a pulverized coal transport line. In the pulverized coal combustion device for supplying and burning the pulverized coal burner, a collector for collecting the fine coal particles discharged from the exhaust pipe of the pulverized coal concentration riser is installed, and collected by the collector. A pulverized coal combustion apparatus, comprising a conduit for connecting the fine coal particles to a fine coal particle injector provided in a burner cylinder of the pulverized coal burner.
【請求項5】請求項4記載の微粉炭燃焼装置において、
微細石炭粒子を捕集する捕集器によって捕集された微細
石炭粒子を、微粉炭バーナに微粉炭を供給する微粉炭輸
送管内に注入する管路を配設したことを特徴とする微粉
炭燃焼装置。
5. The pulverized coal combustion apparatus according to claim 4,
A pulverized coal combustion characterized by having a conduit for injecting the fine coal particles collected by a collector for collecting the fine coal particles into a pulverized coal transport pipe for supplying pulverized coal to a pulverized coal burner. apparatus.
【請求項6】請求項4記載の微粉炭燃焼装置において、
微細石炭粒子を捕集する捕集器がバグフィルタ式捕集器
であることを特徴とする微粉炭燃焼装置。
6. The pulverized coal combustion apparatus according to claim 4,
A pulverized coal combustion apparatus, wherein the collector for collecting fine coal particles is a bag filter type collector.
JP63173939A 1988-07-14 1988-07-14 Pulverized coal burner and pulverized coal combustion device using it Expired - Fee Related JP2738705B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63173939A JP2738705B2 (en) 1988-07-14 1988-07-14 Pulverized coal burner and pulverized coal combustion device using it

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63173939A JP2738705B2 (en) 1988-07-14 1988-07-14 Pulverized coal burner and pulverized coal combustion device using it

Publications (2)

Publication Number Publication Date
JPH0225609A JPH0225609A (en) 1990-01-29
JP2738705B2 true JP2738705B2 (en) 1998-04-08

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Country Link
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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0410217U (en) * 1990-04-26 1992-01-29
JP2020514520A (en) * 2017-01-06 2020-05-21 フェニックス アドバンスド テクノロジーズ リミテッドFenix Advanced Technologies,Limited Portability of solid fuel particles Combustible gas suspension

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5712209A (en) * 1980-06-04 1982-01-22 Foster Wheeler Corp Dual adjusting/double flow burner assembly
JPS6066011A (en) * 1983-09-22 1985-04-16 Ube Ind Ltd Feeder for pulverized coal
JPS60223914A (en) * 1984-04-23 1985-11-08 Kawasaki Heavy Ind Ltd Adjusting device of pulverized coal-air ratio of pulverized coal manufacturing device
JPS6144214A (en) * 1984-08-09 1986-03-03 Mitsubishi Heavy Ind Ltd Fuel particle feeding device
JPS62116810A (en) * 1985-11-14 1987-05-28 Babcock Hitachi Kk Burner device
JPS62210308A (en) * 1986-03-10 1987-09-16 Hitachi Zosen Corp Method of pulverizing coal and supplying the same
JPH01117444U (en) * 1988-01-26 1989-08-08

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