JPS58198606A - Low nox combustion of powdered coal - Google Patents
Low nox combustion of powdered coalInfo
- Publication number
- JPS58198606A JPS58198606A JP8025982A JP8025982A JPS58198606A JP S58198606 A JPS58198606 A JP S58198606A JP 8025982 A JP8025982 A JP 8025982A JP 8025982 A JP8025982 A JP 8025982A JP S58198606 A JPS58198606 A JP S58198606A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- combustion
- fuel ratio
- low
- air
- 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.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
- F23C5/08—Disposition of burners
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
Description
【発明の詳細な説明】
本%131jri電素敵化物(以下NOXと称す)の低
減を図ったボイラりるいは燃焼炉における′rJ11.
粉炭の低NO!燃焼方沃に蘭する。DETAILED DESCRIPTION OF THE INVENTION This 'rJ11.
Low NO of powdered coal! The way it burns is the way it burns.
石民を燃料として用いる石炭焚きボイ/F −*での燃
糎方法は、燃料石炭を微粉化して火炉内に噴出燃焼嘔せ
る微粉炭燃焼が主流でめる。微粉炭燃焼は燃焼用空気に
よって微粉炭を搬送する予混合燃焼法を採用すゐ場合が
多い。バーナより火炉内に噴出された微粉炭は、着火、
熱分解、気体燃焼及び固体燃焼の過程で燃焼を完了する
。燃焼初期領域は着火熱分解の進む領域であり、放出さ
れた揮発分の燃焼領域に移行する。揮発分の多い石炭は
どガス燃焼に近づくために燃焼性が良く、この揮発分の
燃焼火炎によって固体燃焼が助長され、全般的に安定な
燃焼を行なうことができる。従来の燃料石炭は揮発分の
多い石炭を用いてきたが、石炭の輸入を広く海外に依存
するにつれ、揮発分の少ない炭種も含め数多い炭種を燃
料に筐用する傾向になってきている。一般に石炭中に含
有される固定炭素分と揮発分の比は燃料比と称されてい
るが、固定炭素分に比べ揮発分の含有率の高い低燃料比
炭は比較的低温領域で燃焼させることが可能であるが、
固定炭素分に比べ揮発分の含有率の低め高燃料比炭は固
体燃焼を行なわせるためには高温領域で燃焼させること
が必要である。特に固定炭素分の多い石炭燃焼では完全
に燃焼しきれず未燃分が多くなる欠点かめる。・また、
微粉炭燃焼に伴なって生成さfるNOXは石訳中に百M
される菫素分(以下N分と称す)が燃焼過程で酸化され
て生成するフューエルNOXと燃焼用空気中のN分が酸
化さnて生成するサーマルNOXとに大別されるがX
NOX生成鴛の80〜90%はフューエルNOXでめる
。従りて、微粉炭燃焼におけるNOX生成を抑制するた
めにはフューエルNOXを低減する仁とが生体となる。The mainstream combustion method in coal-fired boilers/F-* that uses stone coal as fuel is pulverized coal combustion, in which fuel coal is pulverized and ejected into a furnace for combustion. Pulverized coal combustion often uses a premix combustion method in which the pulverized coal is transported by combustion air. The pulverized coal ejected from the burner into the furnace is ignited,
Combustion is completed through the processes of thermal decomposition, gaseous combustion and solid combustion. The initial combustion region is a region where ignition thermal decomposition progresses, and the region transitions to the combustion region of the released volatile matter. Coal with a high volatile content has good combustibility because it approaches the combustion of gas, and the combustion flame containing this volatile content promotes solid combustion, making it possible to achieve stable combustion overall. Conventional fuel coal has used coal with a high volatile content, but as coal imports have become more dependent on overseas countries, there has been a tendency to use many types of coal as fuel, including those with low volatile content. . Generally, the ratio of fixed carbon content to volatile content contained in coal is called the fuel ratio, but low fuel ratio coal, which has a higher volatile content than fixed carbon content, must be burned in a relatively low temperature range. is possible, but
High fuel ratio coal, which has a lower volatile content than fixed carbon content, needs to be burned in a high temperature range in order to achieve solid combustion. In particular, coal combustion with a high fixed carbon content has the disadvantage that it cannot be completely combusted, leaving a large amount of unburned carbon. ·Also,
The amount of NOx generated during pulverized coal combustion is 100M
It can be broadly divided into fuel NOx, which is produced when the phosphorus content (hereinafter referred to as N content) in the combustion air is oxidized during the combustion process, and thermal NOX, which is produced by the oxidation of the N content in the combustion air.
80 to 90% of the NOX-producing seaweed is produced by fuel NOX. Therefore, in order to suppress NOX generation in pulverized coal combustion, it is necessary to reduce fuel NOX.
従米行なわnている低NOX燃焼法は石炭中N分が熱分
解時に揮発分と共に放出し、酸化さnてtit接NOX
になるものとシアン(HCN)及びアンモニア(NHI
)などN化付物が生成でれる。低酸素雰囲気及び低温領
域でこれらN化付物がNOXをN、に還元することが報
告されている* COi’J Q x還元反応を行なわ
せる条件設定のため低酸素雰囲気を達成させる手段に燃
焼排カスを微粉R燃焼用バーナに鼻儂壊して燃焼させる
方法が報告場れている。この方法に揮発分の多いわ炭に
は有効で6るが罰記し友ごとく、嵩燃料比辰の場せ未燃
分の増加をもたらし、未燃分(固体)の燃焼速度が遅い
ために火炉内で燃焼しきれず排出され、低いNOXは達
成できても未燃分が多くなる欠点がある。従って低NO
X、低未燃分を同時に達成する燃焼法が必要で6る。The low NOx combustion method currently in use is that the nitrogen content in coal is released together with volatile matter during thermal decomposition, oxidizes, and produces NOx in contact with titanium.
and cyanide (HCN) and ammonia (NHI).
) etc. are formed. It has been reported that these nitrogen adducts reduce NOX to N in a low-oxygen atmosphere and low-temperature region. There have been reports of a method in which waste sludge is crushed and burned in a fine powder R combustion burner. Although this method is effective for charcoal with a high volatile content, it has the disadvantage that the bulk fuel ratio increases the unburned content, and the combustion rate of the unburned content (solid) is slow, so the furnace However, even if low NOx can be achieved, there is a disadvantage that there is a large amount of unburned matter. Therefore low NO
X. There is a need for a combustion method that simultaneously achieves low unburned content.
本発明は上記欠点を改譬しようとしてなされたもので、
その目的とするところは、低NOX化と未燃分の排出を
抑制することにある。The present invention was made in an attempt to correct the above-mentioned drawbacks.
The purpose of this is to reduce NOx and suppress emissions of unburned substances.
即ち、本発明の時値とするところは、ボイラ等における
微粉炭の燃焼方法において、微粉炭の噴出部を炉内上下
方向に少なくとも2個所設けると共に、固定炭素分に比
べ揮発分の含有率の低い微粉炭を下方より、また、固定
炭素分に比べ揮発分の含有率の高い微粉炭を上方より夫
々噴出せしめ、かつ、上記揮発分の含有率の低い微粉炭
を理論燃焼空気量以上の空気量過剰の状態で燃焼し、揮
発分の含有率の高い微粉炭は理論燃焼空気量以下の空気
量不足の状態で燃焼せしめてなる微粉炭の低NOX燃焼
方法にある。In other words, in the method of pulverized coal combustion in a boiler or the like, the current value of the present invention is such that at least two pulverized coal injection parts are provided in the vertical direction within the furnace, and the volatile content is lower than the fixed carbon content. Pulverized coal with a low volatile content is ejected from below, and pulverized coal with a high volatile content compared to fixed carbon content is ejected from above, and the pulverized coal with a low volatile content is injected with air in an amount greater than the theoretical combustion air amount. There is a low NOx combustion method for pulverized coal in which pulverized coal is burned in an excess amount and has a high volatile content, and is combusted in an insufficient amount of air that is less than the theoretical combustion air amount.
以下、本発明の一実施例を図面によって説明する。1は
ボイラの火炉、2及び3は火炉1の上下方向に設けられ
た微粉炭燃焼用のバーナであり、固定炭素分に比べ揮発
分の含有率の低い微粉炭(高燃料比炭)4と燃焼用空気
5(予熱され次空気が好ましい)はエゼクタ6で混合さ
れてバーナ2から理論燃焼空気量以上の空気量過剰の状
態で噴出される。また、固定炭素分に比べ揮発分の含有
率の高−ム微粉炭(低燃料比炭)7と燃焼用空気8はエ
ゼクタlOで混合され、排ガス9と共にバーナ3から理
論燃焼空気証以下の空気量不足の状態で噴出される。1
1は火炉1の排ガス通路に設けられて排ガス9t211
11熱する熱交換器でるる、更にAはバーナ2の、また
、Bはバーナ3の燃焼ゾーンである。An embodiment of the present invention will be described below with reference to the drawings. 1 is the furnace of the boiler; 2 and 3 are burners for pulverized coal combustion installed in the vertical direction of the furnace 1; Combustion air 5 (preferably preheated air) is mixed in an ejector 6 and ejected from the burner 2 in an excess amount of air that is greater than the theoretical combustion air amount. In addition, pulverized coal (low fuel ratio coal) 7 with a high volatile content compared to fixed carbon content and combustion air 8 are mixed in the ejector 1O, and air with a temperature below the theoretical combustion air certificate is sent from the burner 3 along with the exhaust gas 9. It is ejected in insufficient quantity. 1
1 is installed in the exhaust gas passage of the furnace 1 and exhaust gas 9t211
In addition, A is the combustion zone of burner 2, and B is the combustion zone of burner 3.
さて、高燃料比炭を火炉1の下方の燃焼シー7人で燃焼
させるようにするので燃焼時間(火炉1内での滞留時間
を長ズすることで未燃分の排出を少なくする。ことがで
きる。燃焼ゾーン人で過剰酸素濃度で高温燃焼をするこ
とで高燃料比炭中のN分が放出し、酸化されてNOXが
生成される。この燃焼ゾーン人は高酸素でしかも高温で
るり、NHl及びHCNの発生量は石炭の種類によって
も異なるがわずかで大中が直接NOXになる。Now, since high fuel ratio coal is combusted in the lower combustion chamber of the furnace 1, the combustion time (residence time in the furnace 1) is lengthened to reduce the emissions of unburned matter. Possible.In the combustion zone, high-temperature combustion with excess oxygen concentration releases the N content in the high fuel ratio coal, which is oxidized and generates NOx. The amount of NHL and HCN generated varies depending on the type of coal, but it is small and large and medium-sized coals directly turn into NOx.
次にバーナ3からはm発鈴の含有率の尚い低燃料比炭7
が供給される。燃焼条件としては石炭供給量に対し燃焼
用空気量が理論燃焼空気量より少ない低空気比で燃焼さ
せる。このような低空気比、すなわち酸素条件で燃焼さ
せるのは燃焼′@度を抑えNO!生成を抑制し、低酸素
雰囲気条件でNH8゜HCNの生成が高酸素条件に比較
して多い友めでめる。低酸素燃焼を行なうため排ガス9
をバーナ3に循壊し、火炉1内に低燃料比炭7と燃焼用
空気8をエゼクタで予め混合した燃料と共に噴出する。Next, from burner 3, low fuel ratio coal 7 with a m-ring content is used.
is supplied. As for combustion conditions, combustion is performed at a low air ratio in which the amount of combustion air is less than the theoretical amount of combustion air relative to the amount of coal supplied. Combustion at such a low air ratio, that is, oxygen conditions, suppresses the combustion rate and is NO! This suppresses the generation of NH8°HCN under low oxygen atmosphere conditions compared to high oxygen conditions. Exhaust gas9 due to low oxygen combustion
is circulated to the burner 3, and is ejected into the furnace 1 together with the low fuel ratio coal 7 and combustion air 8 together with the premixed fuel by the ejector.
この排ガス循環方式は排ガス9が燃焼ゾーンBを包むよ
うにバーナ3から噴出し、外部からの酸素の拡散をなく
シ、低燃料比炭7の燃焼ゾーンBでは常に低酸素条件で
燃焼できるようにしたものでるる、この低燃料比炭7の
燃焼ゾーンBはNH,、HCNが生成して9ることで、
かつ低酸素条件であることから、高燃料比炭4の燃焼ゾ
−ン人で生成したN0XUNHs及びHCNによってN
、r(還元され、jIl終的に火炉lより排出さnるN
OXは抑制することができる。lた、未燃分についても
比較的燃腕性の工くない高燃料比訳4を火ru”iでQ
面一時間を長くするように燃焼させ、燃焼ゾーンBの低
酸素燃焼下で生成した低燃料比炭7かりの未燃分も燃焼
ゾーン人の燃焼での余鯛#!索によって充分火炉l内で
燃焼することができ、未燃分研出も抑制できる。In this exhaust gas circulation system, the exhaust gas 9 is ejected from the burner 3 so as to surround the combustion zone B, eliminating the diffusion of oxygen from the outside, and making it possible to always burn under low oxygen conditions in the combustion zone B of low fuel ratio coal 7. In the combustion zone B of this low fuel ratio coal 7, NH, HCN are generated 9,
In addition, due to the low oxygen conditions, N0XUNHs and HCN produced in the combustion zone of high fuel ratio coal 4 are
, r (reduced, jIl is finally discharged from the furnace l)
OX can be suppressed. In addition, the unburned content is also relatively low in combustibility and has a high fuel ratio.
The unburned sea bream of the low fuel ratio coal produced under low oxygen combustion in combustion zone B is also left over from combustion in the combustion zone! The cables allow sufficient combustion within the furnace l, and also suppress the removal of unburned substances.
不帖明によれは、筒燃料比炭を効率よく燃焼させると同
時に、低燃料比炭を低酸素燃焼させることで南燃料比炭
から生成し′fcN OX’t N *に還元すること
ができ、低NOX%低未燃分會遜成できる効果が必る。According to Fujomei, by efficiently burning cylinder fuel ratio coal and at the same time performing low oxygen combustion of low fuel ratio coal, it is possible to generate from southern fuel ratio coal and reduce it to 'fcN OX't N *. , low NOx%, low unburned fuel, and the effect of achieving low unburned fuel.
図−は杢%明倣粉炭の低NO!燃焼方床の一央ll1A
ガを示すB5?、1図である。
1・・・火炉、2j3・・・バーナ、4・・・*粉炭(
高燃料比炭)、5・・・燃焼用9!気、7・・・値粉畿
(低燃料比炭)、8・・・燃焼用空気。
頁の続き
多発 明 者 菱沼孝夫
日立市幸町3丁目1番1号株式
%式%
1出 願 人 バブコック日立株式会社東京都千代田区
大手町2丁目6
番2号Figure - shows low NO of heather % light imitated powder coal! The center of the combustion bed ll1A
B5 indicating moth? , Figure 1. 1...Furnace, 2j3...Burner, 4...*Powdered coal (
High fuel ratio coal), 5... 9 for combustion! air, 7... value powder (low fuel ratio coal), 8... air for combustion. Many page continuations Akira Takao Hishinuma 3-1-1 Saiwaimachi, Hitachi City Stock % Formula 1 Applicant Babcock Hitachi Co., Ltd. 2-6-2 Otemachi, Chiyoda-ku, Tokyo
Claims (1)
炭の噴出st炉内上下方向に少なくとも2個所数けると
共に、固定炭素分に比べ揮発分の含有率の低い微粉炭を
下方より、また、固定炭素分に比べ揮発分の含有率の商
い微粉炭を上方より夫々噴出せしめ、かつ、上記揮発分
の含有率の低い微粉炭を城鍮燃焼免気菫以上の空気量過
剰の状−で燃焼し、揮発分の含有率の高い微粉炭は塩−
燃焼空気量以下の空気量不足の状態で燃焼せしめてなる
ことを%値とする微粉炭の低NO!燃焼方法。L In the method of combustion of pulverized coal in a boiler etc., the pulverized coal is ejected at at least two places in the vertical direction inside the st furnace, and pulverized coal with a lower content of volatile matter than fixed carbon is added from below. , the pulverized coal with a volatile content compared to the fixed carbon content is spouted from above, and the pulverized coal with a low volatile content is heated in a state with an excess amount of air more than that of a combustion air violet. Pulverized coal that burns and has a high volatile content is salt-
The low NO of pulverized coal is expressed as a percentage when it is combusted in a state where the amount of air is insufficient, which is less than the amount of combustion air! Combustion method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8025982A JPS58198606A (en) | 1982-05-14 | 1982-05-14 | Low nox combustion of powdered coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8025982A JPS58198606A (en) | 1982-05-14 | 1982-05-14 | Low nox combustion of powdered coal |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58198606A true JPS58198606A (en) | 1983-11-18 |
JPS6138961B2 JPS6138961B2 (en) | 1986-09-01 |
Family
ID=13713311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8025982A Granted JPS58198606A (en) | 1982-05-14 | 1982-05-14 | Low nox combustion of powdered coal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58198606A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60245907A (en) * | 1984-05-21 | 1985-12-05 | Hitachi Zosen Corp | Three-stage burner |
WO2002031407A1 (en) * | 2000-10-12 | 2002-04-18 | Asahi Glass Company, Limited | Method for reducing nitrogen oxides in combustion gas from combustion furnace |
JP2004069251A (en) * | 2002-08-09 | 2004-03-04 | Mitsubishi Heavy Ind Ltd | Pulverized coal combustion system |
US7168947B2 (en) * | 2004-07-06 | 2007-01-30 | General Electric Company | Methods and systems for operating combustion systems |
JP2008039341A (en) * | 2006-08-09 | 2008-02-21 | Central Res Inst Of Electric Power Ind | Coal combustion method and coal combustion device |
JP2012215364A (en) * | 2011-04-01 | 2012-11-08 | Mitsubishi Heavy Ind Ltd | Boiler, and method for operating boiler |
US9671108B2 (en) | 2011-04-01 | 2017-06-06 | Mitsubishi Heavy Industries, Ltd. | Combustion burner, solid-fuel-combustion burner, solid-fuel-combustion boiler, boiler, and method for operating boiler |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5881584B2 (en) * | 2012-11-12 | 2016-03-09 | 三菱日立パワーシステムズ株式会社 | boiler |
-
1982
- 1982-05-14 JP JP8025982A patent/JPS58198606A/en active Granted
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60245907A (en) * | 1984-05-21 | 1985-12-05 | Hitachi Zosen Corp | Three-stage burner |
JPH0328641B2 (en) * | 1984-05-21 | 1991-04-19 | Hitachi Shipbuilding Eng Co | |
WO2002031407A1 (en) * | 2000-10-12 | 2002-04-18 | Asahi Glass Company, Limited | Method for reducing nitrogen oxides in combustion gas from combustion furnace |
JP2002115808A (en) * | 2000-10-12 | 2002-04-19 | Asahi Glass Co Ltd | Nitrogen oxide reduction method in combustion gas in combustion furnace |
JP2004069251A (en) * | 2002-08-09 | 2004-03-04 | Mitsubishi Heavy Ind Ltd | Pulverized coal combustion system |
US7168947B2 (en) * | 2004-07-06 | 2007-01-30 | General Electric Company | Methods and systems for operating combustion systems |
JP2008039341A (en) * | 2006-08-09 | 2008-02-21 | Central Res Inst Of Electric Power Ind | Coal combustion method and coal combustion device |
JP2012215364A (en) * | 2011-04-01 | 2012-11-08 | Mitsubishi Heavy Ind Ltd | Boiler, and method for operating boiler |
US9671108B2 (en) | 2011-04-01 | 2017-06-06 | Mitsubishi Heavy Industries, Ltd. | Combustion burner, solid-fuel-combustion burner, solid-fuel-combustion boiler, boiler, and method for operating boiler |
Also Published As
Publication number | Publication date |
---|---|
JPS6138961B2 (en) | 1986-09-01 |
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