JPS63172807A - Method for combustion by pulverized coal burner - Google Patents

Method for combustion by pulverized coal burner

Info

Publication number
JPS63172807A
JPS63172807A JP285587A JP285587A JPS63172807A JP S63172807 A JPS63172807 A JP S63172807A JP 285587 A JP285587 A JP 285587A JP 285587 A JP285587 A JP 285587A JP S63172807 A JPS63172807 A JP S63172807A
Authority
JP
Japan
Prior art keywords
pulverized coal
air
burner
primary air
ratio
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
Application number
JP285587A
Other languages
Japanese (ja)
Inventor
Hiroshi Isobe
礒部 博史
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP285587A priority Critical patent/JPS63172807A/en
Publication of JPS63172807A publication Critical patent/JPS63172807A/en
Pending legal-status Critical Current

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  • Regulation And Control Of Combustion (AREA)

Abstract

PURPOSE:To improve the combustion efficiency of a pulverized coal burner, by decreasing the air/pulverized coal ratio on the burner by separating a pri mary air from a pulverized coal in the neighborhood of the inlet of a burner before they are supplied to the pulverized coal burner and by extracting the primary air only which is separated when the air/pulverized coal ratio is high. CONSTITUTION:The pulverized coal prepared by a coal pulverizer is conveyed by a primary air, passing through a pulverized coal pipe 3, and is fed into the outer pipe 1' of a burner 1 after it is swirled in a vent part 6. When a load is applied and the amount of pulverized coal is decreased, the ratio of pulverized coal to a primary air, that is, the air/pulverized coal ratio is in creased. The pulverized coal is swirled and is separated from the primary air by centrifugal force in the bent part 6 of a pulverized coal pipe 3. Accordingly the air/pulverized coal ratio to be supplied to the burner 1 is changed to be decreased by extracting the primary air only from the pulverized coal pipe 3 through the extracting pipe 7 provided in the vent part 6 when the air/ pulverized coal ratio is getting high. With such an arrangement the combustion efficiency of a burner can be improved.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は微粉炭バーナに供給される空気と微粉炭との比
率が大きくなった場合に微粉炭バーナでの空気/微粉炭
比を小さくして燃焼性を改善するように燃焼させる微粉
炭バーナの燃焼方法に関するものである。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention reduces the air/pulverized coal ratio in a pulverized coal burner when the ratio of air supplied to the pulverized coal burner and pulverized coal becomes large. The present invention relates to a combustion method for a pulverized coal burner in which combustion is performed to improve combustibility.

[従来の技術] 微粉炭バーナとしては、従来、第3図に一例を示す如く
、外筒1の内側に同心状に内筒2を配し、該外筒1の末
端部外側に、微粉炭機(図示せず)に接続した微粉炭管
3の他端に接線方向に接続し、微粉炭機内の微粉炭が1
次空気により微粉炭管3内を搬送されて上記外筒1内に
入り、ここで微粉炭が旋回流となってバーナ先端より噴
出されるようにし、更に、外筒1の先端外周部には2次
空気導入部4があり、該2次空気導入部4より導入され
る2次空気8により上記1次空気十微粉炭Aが燃焼させ
られるようにしである。5は重油バーナである。
[Prior Art] Conventionally, as a pulverized coal burner, as shown in FIG. The pulverized coal pipe 3 is connected tangentially to the other end of the pulverized coal pipe 3 connected to the pulverized coal machine (not shown), and the pulverized coal inside the pulverized coal machine is
Next, the pulverized coal is conveyed through the inside of the pulverized coal pipe 3 by air and enters the above-mentioned outer cylinder 1, where the pulverized coal becomes a swirling flow and is ejected from the tip of the burner. There is a secondary air introduction part 4, and the primary air pulverized coal A is combusted by the secondary air 8 introduced from the secondary air introduction part 4. 5 is a heavy oil burner.

上記構成の微粉炭バーナでの燃焼においては、微粉炭機
から1次°空気によって送られて来る微粉炭がバーナの
外筒1内に接線方向に送り込まれるので、1次空気と微
粉炭は旋回しながらバーナ先端より噴出されて2次空気
導入管4より噴出される2次空気により燃焼させられ、
1次空気と微粉炭の比率、すなわち、空気/微粉炭比が
変化しなければ、良好な燃焼が行われる。
During combustion in the pulverized coal burner with the above configuration, the pulverized coal sent by primary air from the pulverizer is tangentially fed into the outer cylinder 1 of the burner, so the primary air and pulverized coal swirl. while being combusted by secondary air ejected from the tip of the burner and ejected from the secondary air introduction pipe 4,
Good combustion will occur if the ratio of primary air to pulverized coal, ie, the air/pulverized coal ratio, does not change.

[発明が解決しようとする問題点] ところが、微粉炭機で粉砕した微粉炭をただちにバーナ
に送って燃焼される直接燃焼方式では部分負荷になると
、前記1次空気量はあまり変らないのに対し微粉炭量は
減少するため、バーナ部での空気/微粉炭比が大きくな
り、微粉炭の濃度が変って燃焼性が悪くなるという問題
がある。
[Problems to be Solved by the Invention] However, in a direct combustion system in which pulverized coal is pulverized by a pulverizer and immediately sent to a burner for combustion, the amount of primary air does not change much under partial load. Since the amount of pulverized coal decreases, the air/pulverized coal ratio in the burner section increases, causing a problem in that the concentration of pulverized coal changes and combustibility deteriorates.

上記の燃焼性を良くするために、部分負荷時に1次空気
量を減少させて空気/微粉炭比を小さくしようとしても
、微粉炭機の特性、微粉炭管での微粉の堆積防止上から
、微粉炭機内や微粉炭管3内の1次空気量を減少させる
ことは好ましくないので部分負荷での空気/微粉炭比は
下げにくい状況にある。
Even if an attempt is made to reduce the air/pulverized coal ratio by reducing the primary air amount during partial load in order to improve the above-mentioned combustibility, due to the characteristics of the pulverizer and the prevention of fine powder accumulation in the pulverized coal pipe, Since it is not preferable to reduce the amount of primary air inside the pulverized coal machine or the pulverized coal pipe 3, it is difficult to lower the air/pulverized coal ratio under partial load.

そこで、本発明は、バーナに供給される1次空気の一部
をバーナ入口の微粉炭管又はバーナで抽出できるように
して負荷発生時に空気/微粉炭比が大きくなってもバー
ナでの空気/微粉炭比を小さくできて燃焼性が良くなる
ようにしようとするものである。
Therefore, the present invention makes it possible to extract a part of the primary air supplied to the burner by the pulverized coal pipe at the burner inlet or by the burner, so that even if the air/pulverized coal ratio becomes large when a load occurs, the air/pulverized coal ratio at the burner can be extracted. The aim is to reduce the pulverized coal ratio and improve combustibility.

[問題点を解決するための手段] 本発明は、上記目的を達成するために、微粉炭バーナに
供給される1次空気と微粉炭をバーナへの入口部近傍位
置で分離させ、空気/微粉炭比が高いときに上記分離さ
れた1次空気のみ抽気し、バーナでの空気/微粉炭比を
小さくするようにする。
[Means for Solving the Problems] In order to achieve the above object, the present invention separates the primary air and the pulverized coal supplied to the pulverized coal burner at a position near the entrance to the burner, and separates the air/pulverized coal. When the coal ratio is high, only the separated primary air is extracted to reduce the air/pulverized coal ratio in the burner.

[作  用] 微粉炭バーナに供給される1次空気と微粉炭を該バーナ
の入口部近辺で旋回させると、微粉炭は周りに飛ばされ
て1次空気と分離される。
[Function] When the primary air and pulverized coal supplied to the pulverized coal burner are swirled near the inlet of the burner, the pulverized coal is blown around and separated from the primary air.

微粉炭と分離された1次空気を外部に取り出せるように
しておけば、微粉炭バーナでの空気/微粉炭比が大とな
るように変ったときに1次空気のみを抽気すれば、微粉
炭バーナでの空気/微粉炭比を小さくすることができ、
燃焼性を改善することができる。
If the primary air separated from the pulverized coal can be taken out to the outside, when the air/pulverized coal ratio in the pulverized coal burner increases, if only the primary air is extracted, the pulverized coal can be removed. The air/pulverized coal ratio in the burner can be reduced,
Flammability can be improved.

[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例を示すもので、外筒1と内筒
2を2重に配し、外筒1の先端側の外側に2次空気の導
入部4を設けている微粉炭バーナ■に、微粉炭機(図示
せず)から微粉炭管3を経て1次空気十微粉炭へを接線
方向から送入し、外筒1と内筒2どの間で旋回させなが
ら先端より1次空気+微粉炭へを噴出させるようにしで
ある構成において、上記微粉炭管3の微粉炭バーナエ入
口部近くの位置にベンド部6を設け、該ベント部6の内
側に抽気管7を接続し、微粉炭管3を流れる1次空気と
微粉炭がベンド部6で遠心力作用を受けて分離され、1
次空気のi部が抽気管7により抽気されるようにする。
FIG. 1 shows an embodiment of the present invention, in which an outer cylinder 1 and an inner cylinder 2 are arranged in a double layer, and a secondary air introduction part 4 is provided on the outside of the tip side of the outer cylinder 1. Primary air is fed tangentially into the coal burner (1) from a pulverizer (not shown) through the pulverized coal pipe 3, and the coal is rotated between the outer cylinder 1 and the inner cylinder 2 from the tip. In a configuration in which primary air + pulverized coal is blown out, a bend part 6 is provided at a position near the pulverized coal burner inlet of the pulverized coal pipe 3, and an air bleed pipe 7 is connected to the inside of the vent part 6. The primary air and pulverized coal flowing through the pulverized coal pipe 3 are separated by centrifugal force at the bend 6, and
Next, i part of the air is bleeded by the bleed pipe 7.

上記抽気管7は、微粉炭バーナの2次空気導入部4へ接
続して、抽出された1次空気が2次空気としてバーナに
戻されるようにするか、又はバーナ上部の二段燃焼空気
ポートから炉内に投入されるようにする。
The air bleed pipe 7 can be connected to the secondary air introduction part 4 of the pulverized coal burner so that the extracted primary air is returned to the burner as secondary air, or it can be connected to a two-stage combustion air port at the top of the burner. so that it is fed into the furnace from

なお、上記抽気管7の途中には、必要に応じて抽気量を
調節するためダンパ8を設けてもよい。
Note that a damper 8 may be provided in the middle of the air bleed pipe 7 in order to adjust the amount of air bleed as necessary.

微粉炭機にて作り出された微粉炭は、1次空気により搬
送されて微粉炭管3内を通り、ベンド部6で旋回させら
れた後、バーナ■の外筒1内に供給される。負荷が発生
し、微粉炭量が減少すると、上記1次空気と微粉炭との
比率、すなわち、空気/微粉炭比は高くなる。微粉炭管
3のベンド部6では遠心力により微粉炭は飛ばされて1
次空気から分離されるので、上記空気/微粉炭比が高く
なって来ると、ベンド部6の抽気管7より微粉炭管3内
の1次空気のみを抽気し、バーナ■へ供給される空気/
微粉炭化を小さくするように変える。これによりバーナ
での燃焼性が改善される。
The pulverized coal produced by the pulverized coal machine is conveyed by primary air, passes through the pulverized coal pipe 3, is rotated at the bend portion 6, and then supplied into the outer cylinder 1 of the burner (2). When a load is generated and the amount of pulverized coal decreases, the ratio of the primary air to pulverized coal, that is, the air/pulverized coal ratio increases. At the bend 6 of the pulverized coal pipe 3, the pulverized coal is blown away by centrifugal force.
When the air/pulverized coal ratio becomes high, only the primary air inside the pulverized coal pipe 3 is extracted from the air bleed pipe 7 of the bend part 6, and the air is supplied to the burner /
Change to reduce pulverized carbonization. This improves combustibility in the burner.

本発明では、微粉炭管3の終端近く、すなわち、微粉炭
バーナ■の入口部近くで1次空気を抽気して空気/微粉
炭比を小さくするので、微粉炭管3内の1次空気量はベ
ント部6に至るまでは一定であり、微粉炭機内の微粉炭
の搬送効率、微粉炭管内での微粉の堆積防止効果を下げ
ることなく、空気/微粉炭比を小さくすることができる
In the present invention, the primary air is extracted near the end of the pulverized coal pipe 3, that is, near the inlet of the pulverized coal burner (2) to reduce the air/pulverized coal ratio. is constant up to the vent part 6, and the air/pulverized coal ratio can be reduced without reducing the transport efficiency of pulverized coal in the pulverized coal machine and the effect of preventing the accumulation of fine powder in the pulverized coal pipe.

なお、上記実施例において、抽気管7から1次空気を抽
気するのは、空気/微粉炭比が大きくなったときに限ら
ず、常時抽気するようにしてもよい。微粉炭バーナでは
1次空気量に比して微粉炭量が多くなっても支障はない
ためである。又、微粉炭管3のベンド部6に、1次空気
と微粉炭の分離効果を高めるために第1図に示す如くデ
フレクタ9を取り付ければ、1次空気と微粉炭とが遠心
力とデフレクタ9で確実に分離させられ、デフレクタ9
の下流側に抽気管7があるようにすれば、1次空気のみ
が確実に抽気されることになる。
In the above embodiment, the primary air is extracted from the air extraction pipe 7 not only when the air/pulverized coal ratio becomes large, but may be extracted all the time. This is because in a pulverized coal burner, there is no problem even if the amount of pulverized coal becomes larger than the amount of primary air. Furthermore, if a deflector 9 is attached to the bend portion 6 of the pulverized coal pipe 3 as shown in FIG. 1 in order to enhance the effect of separating primary air and pulverized coal, the primary air and pulverized coal will be separated by centrifugal force and deflector 9. Deflector 9
By arranging the air bleed pipe 7 on the downstream side of the air bleed pipe 7, only the primary air can be reliably bled.

次に、第2図は本発明の他の実施例を示すもので、微粉
炭バーナ■の微粉炭入口部に抽気管10を取り付けたも
のである。すなわち、微粉炭バーナエの外筒1と内筒2
との間に微粉炭管3より供給される1次空気士微粉炭は
、旋回流となるように接線方向より供給されるので、該
外筒1と内筒2との間で1次空気と微粉炭は旋回による
遠心力により分離させられ、微粉炭は外側に、1次空気
は内側に集まる。この分離後の1次空気を抽気するため
、内筒2の外側に抽気口11を設け、該抽気口11に抽
気管10を接続した構成とする。
Next, FIG. 2 shows another embodiment of the present invention, in which a bleed pipe 10 is attached to the pulverized coal inlet of the pulverized coal burner (1). That is, the outer cylinder 1 and the inner cylinder 2 of the pulverized coal burner
The primary air pulverized coal supplied from the pulverized coal pipe 3 between the outer cylinder 1 and the inner cylinder 2 is supplied from the tangential direction so as to form a swirling flow. The pulverized coal is separated by the centrifugal force caused by swirling, with the pulverized coal gathering on the outside and the primary air gathering on the inside. In order to bleed the primary air after separation, an air bleed port 11 is provided on the outside of the inner cylinder 2, and an air bleed pipe 10 is connected to the air bleed port 11.

第2図に示した実施例では、バーナ■に入った1次空気
を抽気するので、微粉炭バーナエでの空気/微粉炭比の
変動に素速く対応させることができると共に、バーナ■
での旋回を利用して空気/微粉炭比の高い空気を容易に
抽気できてベンド部6はなくてもよい。又、抽気口11
に図示の如くデフレクタ12を取り付ければ、1次空気
と微粉炭との分離効果を高めることができる。
In the embodiment shown in FIG. 2, the primary air that has entered the burner (2) is extracted, so it is possible to quickly respond to fluctuations in the air/pulverized coal ratio in the pulverized coal burner, and the burner (1)
Air with a high air/pulverized coal ratio can be easily extracted by utilizing the swirling at the pulverized coal, and the bend portion 6 may be omitted. Also, air bleed port 11
If a deflector 12 is attached as shown in the figure, the effect of separating primary air and pulverized coal can be enhanced.

なお、本発明は、上記の各実施例にのみ限定されるもの
ではなく、第1図に示す抽気方式と第2図に示す抽気方
式を併用した構成とし、いずれかの抽気管を利用して空
気/微粉炭比を小さくするようにしてもよい。
It should be noted that the present invention is not limited only to the above-mentioned embodiments, but has a configuration that uses both the air bleed method shown in FIG. 1 and the air bleed method shown in FIG. The air/pulverized coal ratio may be reduced.

[発明の効果] 以上述べた如く、本発明の微粉炭バーナの燃焼方法によ
れば、微粉炭バーナへの1次空気十微粉炭の入口部近傍
位置に、旋回による遠心力で微粉炭を飛ばして分離させ
た1次空気のみを抽気するための装置を備え、微粉炭バ
ーナへ供給される1次空気のみを上記微粉炭入口部近傍
位置で抽気して微粉炭バーナでの空気/微粉炭比を小さ
くするようにしであるので、部分負荷で空気/微粉炭比
が大きくなっても、微粉炭の搬送能力を低下させず微粉
炭管への微粉炭の堆積を防止しながら1次空気量のみを
減少して上記空気/微粉炭比を小さくすることができ、
微粉炭バーナでの燃焼性を改善することができる。
[Effects of the Invention] As described above, according to the pulverized coal burner combustion method of the present invention, pulverized coal is blown to a position near the inlet of the primary air and pulverized coal into the pulverized coal burner by centrifugal force caused by swirling. The device is equipped with a device to bleed only the primary air separated by the pulverized coal burner, and bleeds only the primary air supplied to the pulverized coal burner at a position near the pulverized coal inlet to reduce the air/pulverized coal ratio at the pulverized coal burner. Even if the air/pulverized coal ratio increases due to partial load, the pulverized coal conveyance capacity is not reduced and the amount of pulverized coal is prevented from accumulating in the pulverized coal pipe, while only the primary air amount is maintained. The above air/pulverized coal ratio can be made smaller by reducing
Combustibility in pulverized coal burners can be improved.

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

第1図は本発明の一実施例を示す微粉炭バーナの概略断
面図、第2図は本発明の他の実施例を示す微粉炭バーナ
の概略断面図、第3図は従来の微粉炭バーナの断面図で
ある。 ■・・・微粉炭バーナ、1・・・外筒、2・・・内筒、
3・・・微粉炭管、7,10・・・抽気管。
FIG. 1 is a schematic cross-sectional view of a pulverized coal burner showing one embodiment of the present invention, FIG. 2 is a schematic cross-sectional view of a pulverized coal burner showing another embodiment of the present invention, and FIG. 3 is a schematic cross-sectional view of a pulverized coal burner showing another embodiment of the present invention. FIG. ■...Pulverized coal burner, 1...Outer cylinder, 2...Inner cylinder,
3...Pulverized coal pipe, 7,10...Air bleed pipe.

Claims (1)

【特許請求の範囲】[Claims] 1)微粉炭バーナに1次空気により搬送されて供給され
る微粉炭の上記微粉炭バーナへの入口部近傍位置に、上
記1次空気と微粉炭とを旋回による遠心力で分離させる
部分を設けると共に分離後の1次空気のみを抽気する装
置を設け、微粉炭バーナでの空気/微粉炭比が大きくな
ると、上記抽気装置で1次空気を抽気してバーナ部での
空気/微粉炭比を小さくして燃焼させることを特徴とす
る微粉炭バーナの燃焼方法。
1) A portion is provided near the inlet of the pulverized coal, which is conveyed and supplied to the pulverized coal burner by the primary air, to separate the primary air and the pulverized coal by centrifugal force caused by swirling. At the same time, a device is installed to bleed only the primary air after separation, and when the air/pulverized coal ratio in the pulverized coal burner becomes large, the primary air is extracted with the bleed device to reduce the air/pulverized coal ratio in the burner section. A combustion method using a pulverized coal burner, which is characterized by combustion in a small size.
JP285587A 1987-01-09 1987-01-09 Method for combustion by pulverized coal burner Pending JPS63172807A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP285587A JPS63172807A (en) 1987-01-09 1987-01-09 Method for combustion by pulverized coal burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP285587A JPS63172807A (en) 1987-01-09 1987-01-09 Method for combustion by pulverized coal burner

Publications (1)

Publication Number Publication Date
JPS63172807A true JPS63172807A (en) 1988-07-16

Family

ID=11541002

Family Applications (1)

Application Number Title Priority Date Filing Date
JP285587A Pending JPS63172807A (en) 1987-01-09 1987-01-09 Method for combustion by pulverized coal burner

Country Status (1)

Country Link
JP (1) JPS63172807A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103712227A (en) * 2013-12-13 2014-04-09 山西蓝天环保设备有限公司 High-concentration pulverized coal mixing injection device and method for increasing combustion efficiency
CN105135671A (en) * 2015-09-10 2015-12-09 河南陆德筑机股份有限公司 Multistage air distribution pulverized coal combustion hot blast stove

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103712227A (en) * 2013-12-13 2014-04-09 山西蓝天环保设备有限公司 High-concentration pulverized coal mixing injection device and method for increasing combustion efficiency
CN103712227B (en) * 2013-12-13 2016-08-17 山西蓝天环保设备有限公司 High concentration pulverized coal mixing injection device and the method improving efficiency of combustion
CN105135671A (en) * 2015-09-10 2015-12-09 河南陆德筑机股份有限公司 Multistage air distribution pulverized coal combustion hot blast stove

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