JPH0227291Y2 - - Google Patents

Info

Publication number
JPH0227291Y2
JPH0227291Y2 JP7520885U JP7520885U JPH0227291Y2 JP H0227291 Y2 JPH0227291 Y2 JP H0227291Y2 JP 7520885 U JP7520885 U JP 7520885U JP 7520885 U JP7520885 U JP 7520885U JP H0227291 Y2 JPH0227291 Y2 JP H0227291Y2
Authority
JP
Japan
Prior art keywords
burner
pulverized coal
mixed fuel
inner cylinder
separate plate
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
Application number
JP7520885U
Other languages
Japanese (ja)
Other versions
JPS61192113U (en
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 filed Critical
Priority to JP7520885U priority Critical patent/JPH0227291Y2/ja
Publication of JPS61192113U publication Critical patent/JPS61192113U/ja
Application granted granted Critical
Publication of JPH0227291Y2 publication Critical patent/JPH0227291Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は低負荷時にも安定した燃焼が可能な微
粉炭バーナに関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a pulverized coal burner that is capable of stable combustion even under low load conditions.

[従来の技術] 従来の微粉炭バーナは、微粉炭ミルから一定の
空気量で送られる微粉炭を炉内に噴出させて燃焼
させている。
[Prior Art] A conventional pulverized coal burner injects pulverized coal sent in a constant amount of air from a pulverized coal mill into a furnace and burns it.

[考案が解決しようとする問題点] しかし、微粉炭ミルの負荷が低下すると、該ミ
ルに導入される空気量は一定であるため、空気量
A/微粉炭量Cが増大し、一次空気比が大きくな
り過ぎて燃焼斑が生じ、燃焼が不安定となり、遂
には燃焼不能になつてしまう。
[Problem to be solved by the invention] However, when the load on the pulverized coal mill decreases, since the amount of air introduced into the mill is constant, the amount of air A/the amount of pulverized coal C increases, and the primary air ratio decreases. When the flame becomes too large, combustion spots occur, combustion becomes unstable, and eventually combustion becomes impossible.

[問題点を解決するための手段] 上述の従来の問題点を解決することを日的とし
て本考案では、微粉炭と一次空気の混合燃料を螺
旋状に旋回せしめて導入し、バーナ内筒とバーナ
外筒との間の円筒状流路を通しバーナノズルから
噴出して燃焼させる微粉炭バーナにおいて、前記
混合燃料導入部のバーナ内外筒間に円筒状のセパ
レートプレートを配設し、該混合燃料導入部のセ
パレートプレートとバーナ内筒との間を抽気ライ
ンを介して炉内に接続するようにした。
[Means for Solving the Problems] In order to solve the above-mentioned conventional problems, the present invention introduces a mixed fuel of pulverized coal and primary air in a spiral manner, and connects it to the burner inner cylinder. In a pulverized coal burner that ejects and burns from a burner nozzle through a cylindrical flow path between the burner outer cylinder, a cylindrical separate plate is disposed between the burner inner and outer cylinders of the mixed fuel introduction part, and the mixed fuel is introduced. The separate plate of the section and the burner inner cylinder were connected to the inside of the furnace via a bleed line.

[作用] 比重の重い微粉炭と比重の軽い空気との混合燃
料が、混合燃料導入部で旋回をかけられると、バ
ーナ内外筒間の円筒状流路を流れる間に微粉炭が
外筒側に分離し、円筒側は空気比が増大する。
[Operation] When mixed fuel of pulverized coal with heavy specific gravity and air with light specific gravity is swirled in the mixed fuel introduction section, the pulverized coal flows toward the outer cylinder side while flowing through the cylindrical flow path between the burner inner and outer cylinders. The air ratio increases on the cylindrical side.

抽気ラインにより内筒側の空気を炉内に排出す
ると、バーナノズルから噴出される混合燃料の
A/Cが低下し、微粉炭ミルの負荷が減少しても
常に安定した燃焼が可能になる。
When the air from the inner cylinder side is discharged into the furnace through the bleed line, the A/C of the mixed fuel injected from the burner nozzle is reduced, and stable combustion is always possible even when the load on the pulverized coal mill is reduced.

[実施例] 以下、図面に基づいて本考案の実施例を説明す
る。
[Example] Hereinafter, an example of the present invention will be described based on the drawings.

第1図及び第2図は本考案の一実施例を示すも
ので、1は微粉炭バーナ、2はバーナ内筒、3は
バーナ外筒、4は微粉炭と一次空気との混合燃料
の混合燃料供給管、5は混合燃料導入部、6は円
筒状流路、7はバーナノズル、8はバーナスロー
トであり、混合燃料導入部5の円筒状流路6内に
円筒状のセパレートプレート9を配設する。該セ
パレートプレート9の直径及び長さは、バーナ内
外筒2,3の直径、バーナ出力等に応じて決める
ことができ、例えば直径は、外筒径D及び内筒径
dで表わすとD+d/2、長さは混合燃料供給管4 の径の2倍程度が適当である。
Figures 1 and 2 show an embodiment of the present invention, in which 1 is a pulverized coal burner, 2 is a burner inner cylinder, 3 is a burner outer cylinder, and 4 is a mixture of mixed fuel of pulverized coal and primary air. A fuel supply pipe, 5 is a mixed fuel introduction part, 6 is a cylindrical flow path, 7 is a burner nozzle, 8 is a burner throat, and a cylindrical separate plate 9 is arranged in the cylindrical flow path 6 of the mixed fuel introduction part 5. Set up The diameter and length of the separate plate 9 can be determined depending on the diameters of the burner inner and outer cylinders 2 and 3, the burner output, etc. For example, the diameter is expressed as the outer cylinder diameter D and the inner cylinder diameter d, and is therefore D+d/2. The appropriate length is about twice the diameter of the mixed fuel supply pipe 4.

前記混合燃料導入部5のバーナ内筒2とセパレ
ートプレート9との間の遮蔽板10にバイパス管
11を接続し、該バイパス管11に流量調節ダン
パ12を設け、該バイパス管11を炉内の前記バ
ーナノズル7近傍に開口せしめて抽気ライン13
を構成してある。図中、14はウインドボツク
ス、15は燃焼用空気送給ダクト、16は着火用
の重油バーナを示す。
A bypass pipe 11 is connected to the shielding plate 10 between the burner inner cylinder 2 and the separate plate 9 of the mixed fuel introduction section 5, a flow rate adjustment damper 12 is provided on the bypass pipe 11, and the bypass pipe 11 is connected to the shielding plate 10 between the burner inner cylinder 2 and the separate plate 9. A bleed air line 13 is opened near the burner nozzle 7.
has been configured. In the figure, 14 is a wind box, 15 is a combustion air supply duct, and 16 is a heavy oil burner for ignition.

以上のように構成したので、A/Cの高い混合
燃料が混合燃料導入部5から導入されると、該混
合燃料は円筒状流路6内をバーナ内筒2を中心と
して螺旋状に旋回してバーナノズル7側へ流れ
る。この旋回流によつて遠心力が作用し、比重の
大きい微粉炭が外側(バーナ外筒3側)に集中し
てA/Cが低下し、内側(バーナ内筒2側)は
A/Cが著しく高くなる。
With the above configuration, when the mixed fuel with high A/C is introduced from the mixed fuel introduction part 5, the mixed fuel spirals in the cylindrical flow path 6 around the burner inner cylinder 2. and flows to the burner nozzle 7 side. This swirling flow causes centrifugal force to act, and the pulverized coal with a high specific gravity concentrates on the outside (on the burner outer cylinder 3 side), causing the A/C to decrease, and on the inside (on the burner inner cylinder 2 side), the A/C decreases. significantly higher.

混合燃料は加圧状態で導入されるため、円筒状
流路6内は正圧となり、バイパス管11の流量調
節ダンパ12の開度を大きくすると炉内17の圧
力が相対的に低いことによる圧力差により、バー
ナ内筒2表面のA/Cの著しく高い混合燃料がバ
イパス管11を通つて炉内17のーナノズル7近
傍に流出する。このとき、セパレートプレート9
は排出される空気流と導入される混合燃料との干
渉を防止し、微粉炭濃度の低い空気が分離排出さ
れる。
Since the mixed fuel is introduced in a pressurized state, the inside of the cylindrical flow path 6 becomes positive pressure, and when the opening degree of the flow rate adjustment damper 12 of the bypass pipe 11 is increased, the pressure in the furnace 17 is relatively low. Due to the difference, the mixed fuel with a significantly high A/C on the surface of the burner inner cylinder 2 flows out through the bypass pipe 11 into the furnace interior 17 near the -nano nozzle 7. At this time, separate plate 9
This prevents interference between the discharged air flow and the introduced mixed fuel, and air with a low concentration of pulverized coal is separated and discharged.

バーナノズル7からは、空気量が低減してA/
Cが所定の値まで低下した混合燃料が噴出される
ので、燃焼斑を生ずることなく安定した燃焼が可
能になる。前記バイパス管11から放出される
A/Cの著しく高い混合燃料中の微粉炭も、バー
ナノズル7による火焔により無駄なく燃焼され
る。
From burner nozzle 7, the amount of air is reduced and A/
Since the mixed fuel whose carbon content has decreased to a predetermined value is injected, stable combustion is possible without causing uneven combustion. The pulverized coal in the mixed fuel with extremely high A/C discharged from the bypass pipe 11 is also burnt without waste by the flame from the burner nozzle 7.

なお、本考案の微粉炭バーナは上述の実施例の
みに限定されるものではなく、バイパス管は一本
以上配設することができ、その数はバーナ容量に
応じ定めることができること、バイパス管をバー
ナスロート部に開口させてもよいこと、抽気ライ
ンに吸引装置を設けてもよいこと、等本考案の要
旨を逸脱しない範囲内において種々変更を加え得
ることは勿論である。
It should be noted that the pulverized coal burner of the present invention is not limited to the above-mentioned embodiment, and that one or more bypass pipes can be installed, and the number can be determined according to the burner capacity. Of course, various modifications may be made without departing from the gist of the present invention, such as opening in the burner throat portion or providing a suction device in the bleed line.

[考案の効果] 以上説明したように本考案の微粉炭バーナによ
れば、セパレートプレート及びバイパス管によ
り、微粉炭濃度の低い混合燃料を分離排出するこ
とにより、バーナノズルから噴出される混合燃料
中の微粉炭濃度を高めることができるので、微粉
炭ミルが低負荷の場合にも常に微粉炭濃度を適正
な燃焼域に保持させて安定した燃焼を行わせるこ
とができ、よつて従来は定格の50%負荷が限度で
あつたものが、更に低負荷での燃焼が可能にな
る。
[Effect of the invention] As explained above, according to the pulverized coal burner of the present invention, by separating and discharging the mixed fuel with a low concentration of pulverized coal using the separate plate and bypass pipe, the mixed fuel injected from the burner nozzle is reduced. Since the pulverized coal concentration can be increased, even when the pulverized coal mill is under low load, it can always maintain the pulverized coal concentration in the appropriate combustion range and achieve stable combustion. % load was the limit, but now it is possible to burn at even lower loads.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案の一実施例の説明図、第2図は
第1図は−方向矢視図である。 1は微粉炭バーナ、2はバーナ内筒、3はバー
ナ外筒、5は混合燃料導入部、6は円筒状流路、
7はバーナノズル、9はセパレートプレート、1
1はバイパス管、12は流量調節ダンパ、13は
抽気ラインを示す。
FIG. 1 is an explanatory diagram of an embodiment of the present invention, and FIG. 2 is a view taken in the direction indicated by the arrow in FIG. 1. 1 is a pulverized coal burner, 2 is a burner inner cylinder, 3 is a burner outer cylinder, 5 is a mixed fuel introduction part, 6 is a cylindrical flow path,
7 is a burner nozzle, 9 is a separate plate, 1
1 is a bypass pipe, 12 is a flow rate regulating damper, and 13 is a bleed line.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 微粉炭と一次空気の混合燃料を螺旋状に旋回せ
しめて導入し、バーナ内筒とバーナ外筒との間の
円筒状流路を通しバーナノズルから噴出して燃焼
させる微粉炭バーナにおいて、前記混合燃料導入
部のバーナ内外筒間に円筒状のセパレートプレー
トを配設し、該混合燃料導入部のセパレートプレ
ートとバーナ内筒との間を抽気ラインを介して炉
内に接続してなることを特徴とする微粉炭バー
ナ。
A pulverized coal burner in which a mixed fuel of pulverized coal and primary air is spirally introduced and ejected from a burner nozzle through a cylindrical flow path between a burner inner cylinder and a burner outer cylinder for combustion. A cylindrical separate plate is arranged between the burner inner and outer cylinders of the introduction part, and the separate plate of the mixed fuel introduction part and the burner inner cylinder are connected to the inside of the furnace via a bleed air line. pulverized coal burner.
JP7520885U 1985-05-21 1985-05-21 Expired JPH0227291Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7520885U JPH0227291Y2 (en) 1985-05-21 1985-05-21

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7520885U JPH0227291Y2 (en) 1985-05-21 1985-05-21

Publications (2)

Publication Number Publication Date
JPS61192113U JPS61192113U (en) 1986-11-29
JPH0227291Y2 true JPH0227291Y2 (en) 1990-07-24

Family

ID=30616215

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7520885U Expired JPH0227291Y2 (en) 1985-05-21 1985-05-21

Country Status (1)

Country Link
JP (1) JPH0227291Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0735884B2 (en) * 1987-02-24 1995-04-19 合同製鐵株式会社 Powder fuel supply device for combustion furnace

Also Published As

Publication number Publication date
JPS61192113U (en) 1986-11-29

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