JPS6012522B2 - combustion device - Google Patents
combustion deviceInfo
- Publication number
- JPS6012522B2 JPS6012522B2 JP15409475A JP15409475A JPS6012522B2 JP S6012522 B2 JPS6012522 B2 JP S6012522B2 JP 15409475 A JP15409475 A JP 15409475A JP 15409475 A JP15409475 A JP 15409475A JP S6012522 B2 JPS6012522 B2 JP S6012522B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- combustion chamber
- stage
- air
- primary
- 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
Links
- 238000002485 combustion reaction Methods 0.000 title claims description 145
- 239000000446 fuel Substances 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 26
- 102000004190 Enzymes Human genes 0.000 claims description 15
- 108090000790 Enzymes Proteins 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000000567 combustion gas Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 12
- 239000003638 chemical reducing agent Substances 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000006722 reduction reaction Methods 0.000 description 4
- 238000009841 combustion method Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 235000010005 Catalpa ovata Nutrition 0.000 description 1
- 240000004528 Catalpa ovata Species 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
Description
【発明の詳細な説明】
本発明は燃焼装置に係り、特に燃焼排ガス中の窒素酸化
物の低減を図りうる燃焼装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustion device, and particularly to a combustion device capable of reducing nitrogen oxides in combustion exhaust gas.
各種工場、産業界等において使用されているボィラ等の
燃焼炉において、その燃焼排ガス中に含まれる窒素酸化
物(以下NOxと記載する)の量をできるだけ低い値に
抑制することが社会的に強く要望されている。これは環
境汚染を防止するという社会的要請に応えるもので、こ
の要求は今後さらに厳しくなるものと考えられるが、現
在N○xの規制値としては、燃料中の窒素(N)分が0
.2%である場合、5仰臥下が規定されている。従来か
らボィラ等で実施されている燃焼方法としては二段燃焼
法あるいは再循環ガス注入方式等があり、このような燃
焼方法ではN○x値が100〜15の血であることが一
般的であるが、この値を1/2から1/筑里度の値にま
で低減させることが強く要望されている。第1図及び第
2図は従来技術になる構造のボィラの説明図である。In combustion furnaces such as boilers used in various factories and industries, there is a strong social need to suppress the amount of nitrogen oxides (hereinafter referred to as NOx) contained in the combustion exhaust gas to the lowest possible value. It is requested. This is in response to social demands to prevent environmental pollution, and although this demand is expected to become even stricter in the future, the current regulation value for N○x is that the nitrogen (N) content in fuel is 0.
.. 2%, 5 supine positions are prescribed. Combustion methods conventionally used in boilers include the two-stage combustion method and the recirculation gas injection method, and with these combustion methods, it is common for the N○x value to be 100 to 15. However, it is strongly desired to reduce this value from 1/2 to 1/Chikuri degree. FIG. 1 and FIG. 2 are explanatory diagrams of a boiler having a structure according to the prior art.
第1図及び第2図において、ボィラの燃焼用空気は空気
送風機1で送られ、空気用導管すなわちェアダクト2に
入り、ここで再循環ファン3により燃焼排ガスの一部が
ミキシング装置4から導入、混合される。さらに、混合
されたガスは負荷バーナ用ウィンドボックス5と「三段
熱糠用ウィンドボックス6に適宜配分されて送り込まれ
る。空気を配分する際の微調整は、負荷バーナ用ェアレ
ジスタ7、二段燃焼用ェァレジスタ8により行なわれる
。火炉9内に送り込まれる燃料及び空気は燃焼し、燃焼
排ガスとして、N○x等の有害ガスを排出するものであ
る。なお、仕切板10及び分配ダンパ11は上記ミキシ
ング装置4から導入、混合されたガスを再配分し、上記
負荷バーナ用ウィンドボックス5と上記二J段燃焼用ウ
ィンドボックス6に送り込むために設けられている。こ
のように構成してある従来のボイラにおいて、燃焼排ガ
ス中のN0xを低減するための対策としては、上記負荷
バーナ用ェアレジスタ7からの空気量の不足分を上記二
段燃焼用ェァレジスタ8からの空気を入れて補足し、上
記火炉9内の燃焼反応を遅らせ、火炎温度を下げること
によりN○xの生成量を減らすことが考えられている。1 and 2, the combustion air of the boiler is sent by an air blower 1 and enters an air conduit or air duct 2, where a part of the combustion exhaust gas is introduced from a mixing device 4 by a recirculation fan 3. mixed. Furthermore, the mixed gas is appropriately distributed and sent to the wind box 5 for the load burner and the wind box 6 for the three-stage hot rice bran. This is done by the mixing register 8.The fuel and air sent into the furnace 9 are combusted, and harmful gases such as N○x are discharged as combustion exhaust gas.The partition plate 10 and the distribution damper 11 are It is provided to redistribute the gas introduced and mixed from the device 4 and send it to the load burner wind box 5 and the two-J stage combustion wind box 6.A conventional boiler configured in this way As a measure to reduce NOx in the combustion exhaust gas, air from the two-stage combustion air register 8 is supplemented to compensate for the lack of air from the load burner air register 7, and the amount of air in the furnace 9 is increased. It is considered that the amount of N○x generated can be reduced by slowing down the combustion reaction of the gas and lowering the flame temperature.
従来のボィラの構造によれば、例えば最下段のバーナか
ら上記二段燃焼用ェァレジスタ8までの高さが十分にあ
るため、バーナから出た燃焼は空気不足の状態であり、
かつ高温度の状態にさらされるため、当該燃料が熱分解
、重合等によってカーボナィズ(炭素質化)されてしま
う。一旦カーボナィズした燃料はもカーボナィズしない
燃料と比較すると燃焼速度がより遅くなり、燃焼時間が
長くなって上記火炉9内で燃焼し切れず、低温城にまで
行き、キャリーオーバされた状態となる。この状態では
排ガス中の含塵量が増加し「酵素量が低くならずもした
がってN○xが十分に低減し切れなかったり、あるいは
上記火炉9内のうち、特にバーナ部から当該火炉9の出
口までの距離をより大きくする必要があり、経済的に問
題があった。なお、カーボナィズされない燃料に着目す
れば、一次燃焼により高温となり、一定時間経過した後
、空気過剰な状態である二次燃焼域に送られるため、爆
発状態に近い燃焼を行なう可能性、すなわち高温燃焼に
基づくNOxを増大させる燃焼を行なう可能性があった
。本発明の睦的は上記従来技術の欠点を解決し、効果的
にN○xを低減しつつ未燃分の増大を抑えることができ
る燃焼装置を提供することにある。According to the conventional boiler structure, for example, there is a sufficient height from the lowest burner to the two-stage combustion air register 8, so the combustion coming out of the burner is in an air-starved state.
In addition, since the fuel is exposed to high temperatures, the fuel is carbonized by thermal decomposition, polymerization, etc. Once carbonized, the fuel has a slower combustion speed and a longer combustion time than fuel that is not carbonized, so it cannot be completely burned in the furnace 9, reaches a low temperature, and is carried over. In this state, the amount of dust in the exhaust gas increases, and the amount of enzyme does not decrease, so N○x cannot be reduced sufficiently, or the exit of the furnace 9, especially from the burner section of the furnace 9, There was an economical problem as it required a longer distance from the fuel to the fuel.If we focus on fuel that is not carbonized, the primary combustion results in a high temperature, and after a certain period of time, the secondary combustion occurs in a state where there is an excess of air. The present invention solves the drawbacks of the above-mentioned prior art and has the effect of An object of the present invention is to provide a combustion device that can suppress an increase in unburned components while reducing N○x.
この目的を達成するための本発明の第1の構成は、燃料
の燃焼に必要な酵素量より少ない量の酸素雰囲気で一次
燃焼を行なう一次燃焼室と、該−次燃焼室と運通しかつ
該一次燃焼室で生成した未燃分を二次燃焼させる二次燃
焼室とで火炉を構成し、該二次燃焼室と前記一次燃焼室
との蓮通部へ二J段燃焼用の酵素含有気体を供孫合する
第1の二段燃焼用空気導入手段を設け、前記二次燃焼室
の燃焼ガス後流側へ該二次燃焼室で生成した未燃分を燃
焼させる酵素含有気体を供V給する第2の=J段燃焼用
空気導入手段を謙二次燃焼室に設け、該第2のコ段燃焼
用空気導入手段と前記第1のこJ段燃焼用空気導入手段
は共通のウィンドボックスを有し、前記第2の二J段燃
焼用空気導入手段には酸素含有気体の供給量を調整する
ェアレジスタが設けられていることを特徴とする。また
、本発明の第2の構成は、燃料の燃焼に必要な酵素量よ
り少ない量の酸素雰囲気で鷹伴燃焼を行なう一次燃焼室
と、該一次燃焼室と縮流部を介して運通しかつ該第一次
燃焼室で生成した未燃分を二次燃焼させる二次燃焼室と
で火炉を構成し、前記縮流部へコ段燃焼用の酸素含有気
体を供給するコ段燃焼用空気導入手段を設けたことを特
徴とする。A first configuration of the present invention to achieve this object includes a primary combustion chamber that performs primary combustion in an oxygen atmosphere with an amount of enzyme smaller than the amount of enzyme required for combustion of fuel; A furnace is constituted by a secondary combustion chamber that performs secondary combustion of the unburned content generated in the primary combustion chamber, and enzyme-containing gas for 2J stage combustion is sent to the passage between the secondary combustion chamber and the primary combustion chamber. A first two-stage combustion air introduction means is provided to supply an enzyme-containing gas to the downstream side of the combustion gas of the secondary combustion chamber to combust the unburned content generated in the secondary combustion chamber. A second J-stage combustion air introduction means is provided in the secondary combustion chamber, and the second J-stage combustion air introduction means and the first J-stage combustion air introduction means are provided in a common wind box. The second J-stage combustion air introduction means is characterized in that an air register is provided for adjusting the supply amount of the oxygen-containing gas. Further, the second configuration of the present invention includes a primary combustion chamber in which hawk combustion is performed in an oxygen atmosphere with an amount of enzyme smaller than the amount of enzyme required for combustion of the fuel, and a flow connected to the primary combustion chamber through a condenser section. A furnace is constituted by a secondary combustion chamber that performs secondary combustion of unburned content generated in the primary combustion chamber, and air is introduced for co-stage combustion to supply oxygen-containing gas for co-stage combustion to the condenser section. It is characterized by having a means.
以下、添付の図面を参照し、本発明の燃焼装置の一実施
例について説明する。EMBODIMENT OF THE INVENTION Hereinafter, one embodiment of the combustion apparatus of the present invention will be described with reference to the accompanying drawings.
第3図及び第4図a,bは本発明の一実施例のボィラの
構造説明図で、第3図は主要部の説明図、第4図a,b
はその燃焼機構部A、すなわち負荷バーナ用ウィンドボ
ックス主要部の拡大説明図である。以上の各図において
、一次燃焼室21は二次燃焼室22と共に火炉(主燃焼
室)を構成している。本実施例においては、当該一次燃
焼室21は鷹梓燃焼を行なう複数個のコンパクトなサイ
クロンファーネスで構成されている。また、これら一次
燃焼室21と二次燃焼室22との火炉運通部には図示の
ように縮流部が形成され、該縮流部にはコ段燃焼用空気
の導入口23が設けてあり、また上記二段燃焼室22に
は=J段燃焼用ェアレジスタ24が取付けられている。
なお、この=J段燃焼用空気導入口23と=J段燃焼用
ェアレジスタ24とは共通の二J段燃焼用ウィンドボッ
クス31によって二段燃焼用空気が供給される。上記一
次燃焼室21には負荷バーナ用ウィンドボックス25か
ら燃料の燃焼に必要な酵素量より少ない量の酸素を含有
する燃焼用空気が導入されるが、この際、この燃焼用空
気は負荷バーナ用ェアレジスタ26によって旋回運動が
与えられ、一次燃焼室21に導入されるようになってい
る。3 and 4 a, b are structural explanatory diagrams of a boiler according to an embodiment of the present invention, FIG. 3 is an explanatory diagram of the main parts, and FIG. 4 a, b
is an enlarged explanatory view of the combustion mechanism section A, that is, the main part of the load burner wind box. In each of the above figures, the primary combustion chamber 21 and the secondary combustion chamber 22 constitute a furnace (main combustion chamber). In this embodiment, the primary combustion chamber 21 is constituted by a plurality of compact cyclone furnaces that perform Takazusa combustion. Further, as shown in the figure, a condenser section is formed in the furnace passage section between the primary combustion chamber 21 and the secondary combustion chamber 22, and an inlet 23 for the second-stage combustion air is provided in the constriction section. Furthermore, an air register 24 for =J stage combustion is attached to the two stage combustion chamber 22.
Note that the air for second-stage combustion is supplied to the air inlet 23 for the J-stage combustion and the air register 24 for the J-stage combustion by a common wind box 31 for the second J-stage combustion. Combustion air containing oxygen in an amount smaller than the amount of enzyme required for combustion of fuel is introduced into the primary combustion chamber 21 from the load burner wind box 25. A swirling motion is applied by the air register 26 so that the air is introduced into the primary combustion chamber 21.
複数個の負荷バーナ27は上記負荷バーナ用ェアレジス
タ26の近傍に配備されている。この負荷バーナ27を
点火するに際しては点火トーチ28が利用され、簡単に
点火することが可能である。なお、燃焼用空気は空気送
風機からェアダクト29を経て送られ、ガス再循環ファ
ンから送られる燃焼用排ガスの一部と混合されて上記負
荷バーナ用ェァレジスタ26及び二段燃焼用空気導入口
23を経て送入される。以上説明したように、本実施例
になるボィラは、予燃焼室となる一次燃焼室21と、本
燃焼を行なう二次燃焼室22とを分けることにより二段
に分けて一つの燃焼を行なう構造としたものである。A plurality of load burners 27 are arranged near the load burner air register 26. An ignition torch 28 is used to ignite the load burner 27, and it can be easily ignited. The combustion air is sent from the air blower through the air duct 29, mixed with a portion of the combustion exhaust gas sent from the gas recirculation fan, and then passed through the load burner air register 26 and the two-stage combustion air inlet 23. sent. As explained above, the boiler according to this embodiment has a structure in which one combustion is performed in two stages by separating the primary combustion chamber 21, which serves as a precombustion chamber, and the secondary combustion chamber 22, which performs main combustion. That is.
本実施例においては、一次燃焼室21がコンパクトなサ
イクロンファーネスで構成されているので、燃焼ガス、
空気の損拝が強制的に、かつ効果的に行なわれ、空気量
が十分低くても燃焼が促進される。また、本実施例にお
いては、上記二段燃焼用空気の導入口23が縞流部に設
けられ、しかも各負荷バーナ27直後毎に設けられてい
るので断続的燃焼状態となることが少なく、さらに二段
燃焼用空気が該縮流部により急速混合燈拝されて与えら
れるので、高温かつ低酸素下の状態になる時間が短かい
ため、燃料がカーボナイズされ難い。したがって、ポィ
ラ等燃焼排ガス中のNQ対策を強化することがあっても
、当該排煙ガス中の含塵量が増加することがみられない
。さらにCOガス等、有毒ガスの発生も大幅に抑制する
ことが可能となった。第5図、第6図は本実施例になる
燃焼装置の燃焼効果についてさらにわかり易く説明する
ための説明図で、第5図は比較のために示した従来技術
になるポィラにおける燃焼状況の説明図、第6図は本実
施例になるボィラにおける燃焼状況の説明図である。In this embodiment, since the primary combustion chamber 21 is constituted by a compact cyclone furnace, combustion gas,
The air intake is forced and effective, and combustion is promoted even if the air volume is low enough. Furthermore, in this embodiment, the introduction ports 23 for the two-stage combustion air are provided in the striped flow section, and are also provided immediately after each load burner 27, so that intermittent combustion is less likely to occur. Since the air for second-stage combustion is rapidly mixed and provided by the condenser section, the time under high temperature and low oxygen conditions is short, making it difficult for the fuel to be carbonized. Therefore, even if measures against NQ in combustion exhaust gas such as pollutants are strengthened, the amount of dust in the exhaust gas does not increase. Furthermore, it has become possible to significantly suppress the generation of toxic gases such as CO gas. Fig. 5 and Fig. 6 are explanatory diagrams to more clearly explain the combustion effect of the combustion device according to this embodiment, and Fig. 5 is an explanatory diagram of the combustion situation in the conventional poiler shown for comparison. , FIG. 6 is an explanatory diagram of the combustion situation in the boiler according to this embodiment.
図においてFは火炎を示す。従釆技術になるボィラの場
合、火炎が大きく不完全燃焼の様相を示すのに対し、本
実施例になるボイラでの燃焼では、火炎が小さく、燃焼
が効果的に行なわれることを示している。一方経済面か
らみても、本実施例になる燃焼菱層は構造に特に複雑か
つ高価な部品を要することなく、製造コストの点でも極
めて有利である。In the figure, F indicates flame. In the case of boilers using conventional technology, the flame is large and indicates incomplete combustion, whereas in the case of combustion in the boiler of this example, the flame is small, indicating that combustion is carried out effectively. . On the other hand, from an economic point of view, the combustion diamond layer according to this embodiment does not require particularly complicated and expensive parts in its structure, and is extremely advantageous in terms of manufacturing cost.
本発明の第1の構成を有する燃焼装置の効果は以下のよ
うである。衆知のように、N0xにはサーマルN0xと
フユーエルNOXとがある。サーマルN○xは空気中の
N2が活性化することにより発生するものであるから、
火炎温度を低下させることにより低減することが可能で
ある。しかしながら、フューェルN○xは燃料中の原子
状Nにより発生するものであるから、火炎温度に関係な
く燃焼すれば発生するものである。したがって、フュー
ェルNQを低減するためには発生したN○xを還元剤に
より還元するしかない。この還元剤は燃料中のN分によ
り発生させることが経済的に望ましい。しかし、燃料中
のN分により還元剤を発生させ、N○xを還元するため
には、微妙な02分圧制御が必要である。すなわち、還
元剤の存在時間が極めて短かいことから02の与え方及
び還元反応城を適切にする必要がある。さらに、最終的
には禾燃分を出さないことが燃焼装置として望まれる。
これらの条件をすべて満足させることは従来不可能であ
った。しかし、本発明の第1の構成を有する燃焼装置に
よれば、これらの条件をすべて満たすことが可能となっ
た。すなわち、まず、一次空気と二次空気との空気配分
を制御してトータルとしてのコ段燃焼率を決定し、サ−
マルN○xの発生を抑える。The effects of the combustion device having the first configuration of the present invention are as follows. As is well known, there are two types of NOx: thermal NOx and fuel NOX. Thermal N○x is generated by the activation of N2 in the air, so
It can be reduced by lowering the flame temperature. However, since fuel N○x is generated by atomic N in the fuel, it is generated when the fuel is combusted regardless of the flame temperature. Therefore, the only way to reduce the fuel NQ is to reduce the generated N*x using a reducing agent. It is economically desirable to generate this reducing agent from the N content in the fuel. However, delicate 02 partial pressure control is required to generate a reducing agent from the N component in the fuel and reduce N○x. That is, since the existence time of the reducing agent is extremely short, it is necessary to appropriate the method of providing 02 and the reduction reaction time. Furthermore, it is desired that the combustion device ultimately not emit any fuel.
Conventionally, it has been impossible to satisfy all of these conditions. However, according to the combustion device having the first configuration of the present invention, it has become possible to satisfy all of these conditions. That is, first, the air distribution between primary air and secondary air is controlled to determine the total stage combustion rate, and then the service
Suppress the occurrence of Maru N○x.
次に、一次燃焼室と二次燃焼室の蓮通部へ第1の二段燃
焼用空気導入手段により02を与えることによって、フ
ューヱルN○xと寿命の短かし、還元剤の反応を速やか
に行なわせる。しかも、第1の=J段燃焼用空気導入手
段と第2の二段燃焼用空気導入手段とが共通のウインド
ボックスに設けてあるので、上記した還元反応と完全燃
焼とを同時に満足させるための02の与え方が適切に制
御できる。特に、一次燃焼室を複数個設けた場合には、
二段燃焼によるサーマルN○xの低減と、非常に反応速
度の遠いN○xの還元剤とによる還元反応を同時に達成
することができる。また、本発明の第2の構成を有する
燃焼装置の効果は以下のようである。Next, by supplying 02 to the lotus passages of the primary combustion chamber and the secondary combustion chamber by the first two-stage combustion air introduction means, the life of the fuel N○x is shortened and the reaction of the reducing agent is accelerated. have it done. Moreover, since the first = J-stage combustion air introduction means and the second two-stage combustion air introduction means are provided in a common wind box, it is possible to simultaneously satisfy the above-mentioned reduction reaction and complete combustion. 02 can be appropriately controlled. In particular, when multiple primary combustion chambers are provided,
It is possible to simultaneously achieve a reduction in thermal N○x through two-stage combustion and a reduction reaction using a reducing agent for N○x, which has a very different reaction rate. Further, the effects of the combustion apparatus having the second configuration of the present invention are as follows.
すなわち、一次燃焼室において澄梓燃焼を行なうので、
燃焼ガスおよび空気が強制的に混合燈拝されて少ない空
気で目燃し、空気量が十分低くても燃焼が促進される。
さらに、一次燃焼室と二次燃焼室との火炉連通部に縮流
部を設けたので、該縮流部によりガスが急速混合嬢拝さ
れて燃料のカーボナィズを防止するとともに、還元剤の
まわりに02を均一に存在させ、N○xを効果的に還元
させることができる。このように本発明の効果は顕著で
ある。In other words, since clear azusa combustion is performed in the primary combustion chamber,
Combustion gas and air are forcibly mixed to achieve combustion with a small amount of air, and even if the amount of air is sufficiently low, combustion is promoted.
Furthermore, since a condenser section is provided in the furnace communication section between the primary combustion chamber and the secondary combustion chamber, the gas is rapidly mixed in the condenser section to prevent carbonization of the fuel, and to prevent carbonization of the fuel. By making 02 exist uniformly, N○x can be effectively reduced. As described above, the effects of the present invention are remarkable.
第1図は従来技術になるボィラの説明図で、第2図はそ
の要部である燃焼機構部の説明図L第3図は本発明の一
実施例になるボィラの説明図で、J第4図はその要部と
なる燃焼機構部の説明図、第5図は従釆技術になるボィ
ラにおける燃焼状況の説明図、第6図は本発明の一実施
例になるボィラにおける燃焼状況の説明図である。
1……空気送風機、2,29……ェアダクト、3……ガ
ス再循環ファン、4……ミキシング装置、5,25……
負荷バーナ用ウィンドボックス〜 6,31・・…。
二段燃焼用ウインドボックス、7,26……負荷バーナ
用ェアレジスタ、8,24・・・…=1段燃焼用ェアレ
ジスタ、9・・・・・・火炉「 10,30・・・・・
・仕切板、11……分配ダンパ、21・・・・・・一次
燃焼室、22・…・・二次燃焼室、23・・・・・・二
1段燃焼用空気導入口〜 27・肌・・負荷バーナ、2
8…・・・点火トーチ。氷i図
氷2図
才3図
氷4図
才5図
才6図Fig. 1 is an explanatory diagram of a boiler according to the prior art, Fig. 2 is an explanatory diagram of the combustion mechanism section which is the main part thereof, Fig. 4 is an explanatory diagram of the combustion mechanism that is the main part, Fig. 5 is an explanatory diagram of the combustion situation in a boiler that is a conventional technology, and Fig. 6 is an explanatory diagram of the combustion situation in a boiler that is an embodiment of the present invention. It is a diagram. 1... Air blower, 2, 29... Air duct, 3... Gas recirculation fan, 4... Mixing device, 5, 25...
Wind box for load burner ~ 6,31... Wind box for two-stage combustion, 7, 26...air register for load burner, 8, 24...= air register for first-stage combustion, 9... Furnace 10, 30...
・Partition plate, 11... Distribution damper, 21... Primary combustion chamber, 22... Secondary combustion chamber, 23... Air inlet for 21st stage combustion ~ 27. Skin ...Load burner, 2
8...Ignition torch. Ice i figure Ice 2 figure Age 3 figure Ice 4 figure Age 5 figure Age 6 figure
Claims (1)
気で一次燃焼を行なう一次燃焼室と、該一次燃焼室と連
通しかつ該一次燃焼室で生成した未燃分を二次燃焼させ
る二次燃焼室とで火炉を構成し、該二次燃焼室と前記一
次燃焼室との連通部へ二段燃焼用の酵素含有気体を供給
する第1の二段燃焼用空気導入手段を設け、前記二次燃
焼室の燃焼ガス後流側へ該二次燃焼室で生成した未燃分
を燃焼させる酵素含有気体を供給する第2の二段燃焼用
空気導入手段を該二次燃焼室に設け、該第2の二段燃焼
用空気導入手段と前記第1の二段燃焼用空気導入手段は
共通のウインドボツクスを有し、前記第2の二段燃焼用
空気導入手段には酸素含有気体の供給量を調整するエア
レジスタが設けられていることを特徴とする燃焼装置。 2 燃料の燃焼に必要な酵素量より少ない量の酵素雰囲
気下で撹拌燃焼を行なう一次燃焼室と、該一次燃焼室と
縮流部を介して連通しかつ該一次燃焼室で生成した未燃
分を二次燃焼させる二次燃焼室とで火炉を構成し、前記
縮流部へ二段燃焼用の酵素含有気体を供給する二段燃焼
用空気導入手段を設けたことを特徴とする燃焼装置。[Scope of Claims] 1. A primary combustion chamber that performs primary combustion in an enzyme atmosphere with an amount of enzyme smaller than that required for combustion of fuel, and a primary combustion chamber that communicates with the primary combustion chamber and removes unburned matter generated in the primary combustion chamber. A first two-stage combustion air introduction which constitutes a furnace with a secondary combustion chamber for performing secondary combustion, and supplies an enzyme-containing gas for two-stage combustion to a communication portion between the secondary combustion chamber and the primary combustion chamber. a second two-stage combustion air introducing means for supplying an enzyme-containing gas for burning unburned matter generated in the secondary combustion chamber to the downstream side of the combustion gas of the secondary combustion chamber; provided in the combustion chamber, the second two-stage combustion air introduction means and the first two-stage combustion air introduction means have a common window box, and the second two-stage combustion air introduction means has a common window box. A combustion device characterized by being provided with an air register that adjusts the amount of oxygen-containing gas supplied. 2. A primary combustion chamber that performs stirring combustion in an enzyme atmosphere with an amount of enzyme less than that required for combustion of fuel, and unburned matter that is in communication with the primary combustion chamber via a condenser section and that is generated in the primary combustion chamber. A combustion apparatus comprising a furnace comprising a secondary combustion chamber for secondary combustion, and a second-stage combustion air introducing means for supplying enzyme-containing gas for second-stage combustion to the condenser section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15409475A JPS6012522B2 (en) | 1975-12-25 | 1975-12-25 | combustion device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15409475A JPS6012522B2 (en) | 1975-12-25 | 1975-12-25 | combustion device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5278127A JPS5278127A (en) | 1977-07-01 |
| JPS6012522B2 true JPS6012522B2 (en) | 1985-04-02 |
Family
ID=15576765
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15409475A Expired JPS6012522B2 (en) | 1975-12-25 | 1975-12-25 | combustion device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6012522B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5938511A (en) * | 1982-08-26 | 1984-03-02 | Babcock Hitachi Kk | Multistage combustion |
-
1975
- 1975-12-25 JP JP15409475A patent/JPS6012522B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5278127A (en) | 1977-07-01 |
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