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JPS6026922B2 - pulverized coal burner - Google Patents

pulverized coal burner

Info

Publication number
JPS6026922B2
JPS6026922B2 JP2241380A JP2241380A JPS6026922B2 JP S6026922 B2 JPS6026922 B2 JP S6026922B2 JP 2241380 A JP2241380 A JP 2241380A JP 2241380 A JP2241380 A JP 2241380A JP S6026922 B2 JPS6026922 B2 JP S6026922B2
Authority
JP
Japan
Prior art keywords
throat
pulverized coal
primary
air
flame
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
JP2241380A
Other languages
Japanese (ja)
Other versions
JPS56119406A (en
Inventor
皎 出羽
知行 信濃
佑芳 芝山
親利 蔵田
健一 藤井
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP2241380A priority Critical patent/JPS6026922B2/en
Priority to GB8105295A priority patent/GB2070761B/en
Priority to DE19813106824 priority patent/DE3106824C2/en
Priority to DE19818105115 priority patent/DE8105115U1/en
Publication of JPS56119406A publication Critical patent/JPS56119406A/en
Publication of JPS6026922B2 publication Critical patent/JPS6026922B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel
    • F23D1/02Vortex burners, e.g. for cyclone-type combustion apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/01001Pulverised solid fuel burner with means for swirling the fuel-air mixture

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Description

【発明の詳細な説明】 本発明は、徴粉炭燃焼に於けるN0x生成量の低減、安
定燃焼、C○,未燃カーボンの減少を図ることのできる
徴粉炭バーナに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pulverized coal burner that is capable of reducing the amount of NOx produced during pulverized coal combustion, stable combustion, and reduction of CO and unburned carbon.

近時、低N0x用の徴粉炭バーナとして、第1図に示す
如く1次スロート1内の先端部に同心に徴粉炭分散用ス
ワラー2を設け、1次スロート1の外周側に同心に2次
スロート3を設け、2次スロート3の外周側に同心にバ
ーナスロート4を設けて成るものがある。
Recently, as a pulverized coal burner for low N0x, a pulverized coal dispersion swirler 2 is installed concentrically at the tip of the primary throat 1 as shown in Fig. There is one in which a throat 3 is provided and a burner throat 4 is provided concentrically on the outer circumferential side of the secondary throat 3.

かかる構造の低NQ用微粉炭バーナでは、徴粉炭が1次
スロート「1を通して1次空気によって毅送され、スワ
ラー2によって旋回しつつ炉中に吹出される。
In a pulverized coal burner for low NQ having such a structure, pulverized coal is forced by the primary air through the primary throat ``1'' and is blown into the furnace while being swirled by the swirler 2.

2次空気は2次スロート3より旋回しないで吹出され、
3次空気はバーナスロート4より旋回するように吹出さ
れる。
The secondary air is blown out from the secondary throat 3 without swirling,
The tertiary air is blown out from the burner throat 4 in a swirling manner.

そしてスワラー2を通して旋回しつつ吹出された徴粉炭
は1次空気により燃焼せしめられて1次火炎5が形成さ
れ、この1次火炎の燃焼による禾燃分が2次スロート3
,バーナスロート4より吹出された2次空気及び3次空
気により燃焼せしめられて2次火炎6が形成される。前
記1次,2.次,3次空気は夫々徴粉炭全体の必要燃焼
空気量を分散したものであるが、′1次空気及び徴粉炭
に強い旋回が与えられている為、2次空気及び3次空気
と速やかに混合し、急速燃焼,してN○xの生成量が効
果的には低下しない。一方、1次空気及び徴粉炭の旋回
を緩めて、2次空気,3次空気との急速な混合を避ける
構造とすれば火炎の保炎性能が低下して燃焼の安定性が
矢なわれて、C○,禾燃カーボンの発生が増大するとい
う問題がある。
The pulverized coal that is blown out while swirling through the swirler 2 is combusted by the primary air to form a primary flame 5.
, the secondary air and tertiary air blown out from the burner throat 4 cause combustion, and a secondary flame 6 is formed. Said primary, 2. The secondary and tertiary air are obtained by dispersing the amount of combustion air required for the entire pulverized coal, but because the primary air and pulverized coal are given a strong swirl, they are quickly combined with the secondary air and tertiary air. Mixing and rapid combustion do not effectively reduce the amount of N○x produced. On the other hand, if the swirling of the primary air and pulverized coal is loosened to avoid rapid mixing with the secondary and tertiary air, the flame holding performance will decrease and the stability of combustion will suffer. , C○, there is a problem that the generation of combustion carbon increases.

本発明はかかる諸事情に鑑みなされたものであり、前述
の低N○x散粉炭バーナの機造上の問題点を究明し、こ
れを鱗決すべく大中に改良して、徴粉炭の燃焼に於ける
NQの生成量を大中に低減し、保炎を良好にして安定燃
焼させ、C○,未燃カーボンを減少させて燃焼効率を良
好にして、排ガス中のN○x濃度を大坪劇こ低減するこ
とができるようになした超低N○x用の徴粉炭バ−ナを
提供せんとするものである。
The present invention has been made in view of these circumstances, and has investigated the mechanical problems of the low N○x pulverized coal burner described above, and improved the structure to solve the problem. It greatly reduces the amount of NQ generated in the exhaust gas, improves flame holding, and achieves stable combustion, reduces C○ and unburned carbon, improves combustion efficiency, and greatly reduces the N○x concentration in exhaust gas. It is an object of the present invention to provide a pulverized coal burner for ultra-low N○x that can dramatically reduce the amount of nitrogen.

以下本発明による徴粉炭バーナの構造を第2図及び第3
図によって説明すると、1は1次空気と徴粉炭を供給す
る1次スロートで、該1次スロート1内の先端に徴粉炭
分散用スワラ−2が同0に配設されている。
The structure of the pulverized coal burner according to the present invention is shown in Figs. 2 and 3 below.
To explain with reference to the drawings, reference numeral 1 denotes a primary throat for supplying primary air and fine coal, and a swirler 2 for dispersing fine coal is disposed at the tip within the primary throat 1.

前記1次スロート1の先端には外方に拡開せる保炎板7
が一体に設けられており、1次スロート1の外周側には
同○‘こ2次空気を供給する2次スロート3が進退可能
に設けられている。
At the tip of the primary throat 1, there is a flame holding plate 7 that can expand outward.
A secondary throat 3 for supplying secondary air is provided on the outer peripheral side of the primary throat 1 so as to be movable forward and backward.

2次スロート3の外周側には3次空気を供v給するバー
ナスロート4′が設けられ、該バーナスロート4′はデ
ィフューザ型になされている。
A burner throat 4' for supplying tertiary air is provided on the outer peripheral side of the secondary throat 3, and the burner throat 4' is shaped like a diffuser.

尚8は、旋回羽根で、バーナスロート4′から吹出す3
次空気を旋回させる為のものである。
In addition, 8 is a swirl vane, and 3 blows out from the burner throat 4'.
This is to swirl the air.

かように構成された本発明の徴粉炭バーナに於いて、徴
粉炭は1次スロート1を通して1次空気によって搬送さ
れ、スワラー2によって緩く旋回しつつ炉中に吹出され
る。一方、2次空気,3次空気は保炎板7で外方に向け
られる為、徴粉炭と2次空気,3次空気との混合が抑制
され、1次空気によって緩慢に低温燃焼し、1次火炎5
が形成される。従って1次火炎5は極端に02不足の燃
焼となり、NQの生成が著しく低減される。またこの1
次火炎5は主として02不足状態での徴粉炭の揮発分の
低温燃焼であるので脱硝反応を起こすチャー及び未燃成
分(炭化水素,NH3,HCN,CO等)が生成され、
これがN○xと反応してN○xを最終的にはN2に還元
することになる。保炎板7により外側に向って流れる2
次空気及び3次空気は、デイフューザ型のバーナスロー
ト4′の外方に拡関する先端都内周面に案内されてスム
ーズに流れ、1次火炎5の先方で該1次火炎5における
相当量の未燃分であるチャ−と混合し、チャ−を緩慢に
低温燃焼させ、2次火炎6を形成する。この2次火炎6
におけるチャーの緩慢な低温燃焼によりNQが、生成さ
れるが、これと同時に前記未燃成分も生成され、炉内に
広く分布し、長く滞留するので、この未燃成分によって
NQの還元反応が促進され、NQ濃度が低減されると共
に未燃分の燃焼も徐々に行なわれてその濃度が減少する
。然して本発明の徴粉炭バーナでは、2次スロート3を
進退可能になしてあるので、前記徴粉炭燃鱗において2
次スロート3を進退させることにより2次空気の吹出し
量を減少したり増加したりすることができると共に2次
空気及び3次空気の流れを変えることができるので、2
次火炎6におけるチャーの燃焼を低N0xと燃焼効率の
面から最良条件で行なうことができる。
In the pulverized coal burner of the present invention constructed as described above, the pulverized coal is conveyed by the primary air through the primary throat 1, and is blown into the furnace while being gently swirled by the swirler 2. On the other hand, since the secondary air and tertiary air are directed outward by the flame-holding plate 7, mixing of the fine coal with the secondary air and tertiary air is suppressed, and the primary air causes slow low-temperature combustion, resulting in 1 Next flame 5
is formed. Therefore, the primary flame 5 burns with an extremely insufficient amount of 02, and the generation of NQ is significantly reduced. Also this one
The secondary flame 5 is mainly a low-temperature combustion of volatile components of pulverized coal in an 02-deficient state, so char and unburned components (hydrocarbons, NH3, HCN, CO, etc.) that cause a denitrification reaction are generated.
This reacts with N○x and ultimately reduces N○x to N2. Flowing outward by the flame holding plate 7 2
The secondary air and tertiary air flow smoothly while being guided by the outwardly expanding tip inner peripheral surface of the diffuser-type burner throat 4', and a considerable amount of unused air in the primary flame 5 is removed at the tip of the primary flame 5. It mixes with char, which is a fuel, and slowly burns the char at a low temperature to form a secondary flame 6. This secondary flame 6
NQ is generated by the slow, low-temperature combustion of the char, but at the same time, the unburned components are also generated, which are widely distributed in the furnace and remain for a long time, so that the reduction reaction of NQ is promoted by these unburned components. As a result, the NQ concentration is reduced, and the unburned matter is gradually burned, resulting in a decrease in the NQ concentration. However, in the pulverized coal burner of the present invention, since the secondary throat 3 is movable back and forth, the pulverized coal burner has two
By moving the secondary throat 3 forward and backward, the amount of secondary air blown out can be decreased or increased, and the flow of secondary air and tertiary air can be changed.
The combustion of char in the secondary flame 6 can be performed under the best conditions in terms of low NOx and combustion efficiency.

以上詳記した通り本発明の徴粉炭バーナは、1次スロー
トを通して1次空気によって搬送され、スワラーによっ
て緩く旋回しつつ炉中に吹出される徴粉炭は2次スロー
トから吹出される2次空気及びディフューザ型のバーナ
スロートから吹出される3次空気が外方に拡開せる保炎
板により外側に向って流れ且つバーナスロートの先端都
内面に沿って1次火炎の先方に流れるので緩慢な02不
足の低温燃焼となり、NQの生成量が減少する。
As detailed above, in the pulverized coal burner of the present invention, the pulverized coal is conveyed by primary air through the primary throat and blown into the furnace while being gently swirled by the swirler, and the pulverized coal is blown into the furnace by the secondary air blown out from the secondary throat. The tertiary air blown out from the diffuser-type burner throat flows outward by the flame holding plate that expands outward, and flows ahead of the primary flame along the inner surface of the tip of the burner throat, resulting in a slow 02 shortage. This results in low-temperature combustion, and the amount of NQ produced decreases.

また保炎板により保炎も充分なされるので失火すること
がない。また2次空気及び3次空気は、1次火炎の下流
で1次火炎における相当量の未燃分であるチャーと混合
して緩慢に低温燃焼するので2次火炎でのNQ生成も低
減される。また徴粉炭はスワラーにより旋回が与えられ
ている為、2次火炎領域では炉内に適当に分散し2次空
気,3次空気と広い領域で拡散燃焼を行なう為、極めて
燃焼効率が良く、C0,未燃カーボンが著しく減少する
。さらに2次スロートが進退可能となっていて、2次空
気量及び2次,3次空気の流れをコントロールすること
ができるので、2次火炎の燃焼を低NQを燃焼効率の面
から最良の条件で行なうことができる。
In addition, the flame holding plate ensures sufficient flame holding, so misfires do not occur. In addition, secondary air and tertiary air mix with char, which is a considerable amount of unburned matter in the primary flame, downstream of the primary flame and burn slowly and at low temperature, so NQ generation in the secondary flame is also reduced. . In addition, since the pulverized coal is swirled by a swirler, it is properly dispersed in the furnace in the secondary flame area and diffuse combustion is performed in a wide area with the secondary air and tertiary air, resulting in extremely high combustion efficiency and CO , unburned carbon is significantly reduced. Furthermore, the secondary throat can move forward and backward, and the amount of secondary air and the flow of secondary and tertiary air can be controlled, so the combustion of the secondary flame is achieved under the best conditions in terms of low NQ and combustion efficiency. It can be done with

従って本発明の徴粉炭バーナは、その徴粉炭燃焼が超低
NQ燃焼となって、NQの生成が著しく低減し、且つ安
定した効率の良い燃焼となって、C0,未燃カーボンが
著しく減少するという優れた効果がある。
Therefore, in the pulverized coal burner of the present invention, the pulverized coal combustion becomes ultra-low NQ combustion, the generation of NQ is significantly reduced, and the combustion is stable and efficient, resulting in a significant reduction in CO and unburned carbon. This has an excellent effect.

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

第1図は従釆の徴粉炭バーナを示す縦断面図、第2図は
本発明による徴粉炭バーナを示す縦断面図である。 1・・・・・・1次スロート、2・・・・・・徴粉炭分
散用スワフー、3……2次スロート、4′……デイフュ
ーザ型のバーナスロート、5・・・・・・1次火炎、6
・・・・・・2次火炎、7・・・・・・保炎板、8・・
・・・・旋回羽根。 第1図第2図
FIG. 1 is a longitudinal sectional view showing a secondary pulverized coal burner, and FIG. 2 is a longitudinal sectional view showing a pulverized coal burner according to the present invention. 1...Primary throat, 2...Swahoo for dispersing pulverized coal, 3...Secondary throat, 4'...Diffuser type burner throat, 5...Primary flame, 6
...Secondary flame, 7...Flame holding plate, 8...
...Swirl blade. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1 微粉炭バーナに於いて、1次スロートの先端に外方
に拡開せる保炎板を一体に設け、1次スロートの外周側
に同心に設けられた2次スロートを進退可能になし、2
次スロートの外周側に設けられたバーナスロートをデイ
フユーザ型になしたことを特徴とする微粉炭バーナ。
1. In a pulverized coal burner, a flame holding plate that can expand outward is integrally provided at the tip of the primary throat, and the secondary throat, which is provided concentrically on the outer circumference of the primary throat, can be moved back and forth;
A pulverized coal burner characterized in that the burner throat provided on the outer peripheral side of the secondary throat is of a diffuser type.
JP2241380A 1980-02-25 1980-02-25 pulverized coal burner Expired JPS6026922B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2241380A JPS6026922B2 (en) 1980-02-25 1980-02-25 pulverized coal burner
GB8105295A GB2070761B (en) 1980-02-25 1981-02-19 Pulverized coal burner
DE19813106824 DE3106824C2 (en) 1980-02-25 1981-02-24 Pulverized coal burners
DE19818105115 DE8105115U1 (en) 1980-02-25 1981-02-24 CARBON DUST BURNER

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2241380A JPS6026922B2 (en) 1980-02-25 1980-02-25 pulverized coal burner

Publications (2)

Publication Number Publication Date
JPS56119406A JPS56119406A (en) 1981-09-19
JPS6026922B2 true JPS6026922B2 (en) 1985-06-26

Family

ID=12081972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2241380A Expired JPS6026922B2 (en) 1980-02-25 1980-02-25 pulverized coal burner

Country Status (3)

Country Link
JP (1) JPS6026922B2 (en)
DE (2) DE3106824C2 (en)
GB (1) GB2070761B (en)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4412814A (en) * 1981-12-21 1983-11-01 Dennis Jr Silas P Apparatus and method for operating a brick kiln
DE3331989A1 (en) * 1983-09-05 1985-04-04 L. & C. Steinmüller GmbH, 5270 Gummersbach METHOD FOR REDUCING NO (DOWN ARROW) X (DOWN ARROW) EMISSIONS FROM THE COMBUSTION OF NITROGENOUS FUELS
GB8324644D0 (en) * 1983-09-14 1983-10-19 Boc Group Plc Apparatus for burning fuel
JPS6064110A (en) * 1983-09-20 1985-04-12 Babcock Hitachi Kk Low nox burner
JPS60191103A (en) * 1984-03-13 1985-09-28 Babcock Hitachi Kk Burning method of lower rate of nox in combustion gas
GB2165633A (en) * 1984-10-11 1986-04-16 Air Prod & Chem Pulverent fuel burner
JPS6169608U (en) * 1984-10-15 1986-05-13
GB8530734D0 (en) * 1985-12-13 1986-01-22 Peabody Holmes Ltd Burner
JPH0754162B2 (en) * 1986-05-26 1995-06-07 株式会社日立製作所 Burner for low NOx combustion
US4946382A (en) * 1989-05-23 1990-08-07 Union Carbide Corporation Method for combusting fuel containing bound nitrogen
DE3936105C2 (en) * 1989-10-30 1994-12-22 Guenter Dr Ing Slowik Swirl generator for swirl burner
FI98658C (en) * 1990-03-07 1997-07-25 Hitachi Ltd Burner for pulverized carbon, boiler for pulverized carbon and method for combustion of pulverized carbon
JP2565620B2 (en) * 1992-06-15 1996-12-18 株式会社日立製作所 Combustion method of pulverized coal
US5680823A (en) * 1995-03-22 1997-10-28 The Babcock & Wilcox Company Short flame XCL burner
DK173204B1 (en) * 1997-03-07 2000-03-13 F.L.Smidth & Co A/S is in an oven Proceed and burn to introduce burning
JP3344694B2 (en) * 1997-07-24 2002-11-11 株式会社日立製作所 Pulverized coal combustion burner
JP2000257811A (en) * 1999-03-03 2000-09-22 Hitachi Ltd Method and device for burning pulverized coal, and pulverized coal burning burner
JP4261401B2 (en) * 2004-03-24 2009-04-30 株式会社日立製作所 Burner, fuel combustion method and boiler remodeling method
FR2888899A1 (en) * 2005-07-21 2007-01-26 Egci Pillard Sa ANNULAR PIPE ASSEMBLY AND BURNER COMPRISING SUCH AN ASSEMBLY
EP2141413A1 (en) * 2008-12-22 2010-01-06 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method for oxycombustion of pulverized solid fuels
JP5897363B2 (en) * 2012-03-21 2016-03-30 川崎重工業株式会社 Pulverized coal biomass mixed burner
JP5897364B2 (en) * 2012-03-21 2016-03-30 川崎重工業株式会社 Pulverized coal biomass mixed burner
EP3060845A4 (en) * 2013-10-21 2017-07-05 Hatch Ltd Velocity control shroud for burner
JP6231047B2 (en) * 2015-06-30 2017-11-15 三菱日立パワーシステムズ株式会社 Solid fuel burner

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB704901A (en) * 1951-08-07 1954-03-03 Pollopas Patents Ltd Improvements in or relating to pulverised fuel burners, more particularly for cementkilns and similarly constructed furnaces
US3788796A (en) * 1973-05-09 1974-01-29 Babcock & Wilcox Co Fuel burner

Also Published As

Publication number Publication date
DE8105115U1 (en) 1981-10-01
DE3106824C2 (en) 1985-03-14
JPS56119406A (en) 1981-09-19
GB2070761A (en) 1981-09-09
DE3106824A1 (en) 1981-12-03
GB2070761B (en) 1984-06-13

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