JPS6231247B2 - - Google Patents
Info
- Publication number
- JPS6231247B2 JPS6231247B2 JP57004852A JP485282A JPS6231247B2 JP S6231247 B2 JPS6231247 B2 JP S6231247B2 JP 57004852 A JP57004852 A JP 57004852A JP 485282 A JP485282 A JP 485282A JP S6231247 B2 JPS6231247 B2 JP S6231247B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- chamber
- primary
- air
- fuel
- 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
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
- F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
- F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
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)
Description
【発明の詳細な説明】
この発明は、燃料の燃焼において燃焼の改善を
はかるため、いわゆる2段燃焼法の燃焼面の制約
を除き、窒素酸化物およびばいじんの抑制にきわ
めて効果的な2段燃焼を可能にした耐火材類で構
成された還元室を介装したガス化燃焼装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION In order to improve combustion in fuel combustion, the present invention eliminates the combustion limitations of the so-called two-stage combustion method, and employs two-stage combustion, which is extremely effective in suppressing nitrogen oxides and soot. The present invention relates to a gasification combustion device equipped with a reduction chamber made of refractory materials that makes it possible to achieve this.
窒素酸化物NOxの発生には、(1)空気中の窒素
の酸化による場合(Thearmal NOx)と(2)燃料中
の窒素が燃焼によつて酸化する場合(Fuel
NOx)の2つの要因が一般に知られているが、
最近の研究により(3)2段燃焼の場合のように還元
雰囲気の1次燃焼で発生したアンモニア(NH3)
シアン(CN)2等の中間生成物が2次燃焼で酸化
される場合(Combastion NOx)の要因が明らか
になつている。 Nitrogen oxide NOx is generated by (1) oxidation of nitrogen in the air (Thermal NOx) and (2) oxidation of nitrogen in fuel by combustion (Fuel NOx).
Two factors are generally known for NOx),
Recent research shows that (3) ammonia (NH 3 ) generated during the primary combustion in a reducing atmosphere, such as in the case of two-stage combustion;
The causes of oxidation of intermediate products such as cyanide (CN) 2 during secondary combustion (Combastion NOx) have been clarified.
このような発生機構からNOxを低減できる有
効な方法として、たとえば大型発電ボイラなどで
2段燃焼法が行なわれている。 As an effective method for reducing NOx from such a generation mechanism, a two-stage combustion method is used, for example, in large power generation boilers.
しかし、この種の2段燃焼法では、燃焼室で1
次空気量を少なくするほど窒素酸化物抑制効果が
大きいが1次燃焼域での酸素濃度が低下し、その
領域での燃焼温度が下がり、燃料と空気の混合が
悪化することから燃焼が悪化して未燃分が増加
し、ばいじんの著増を伴なうという燃焼面からの
制約があるため、窒素酸化物抑制効果をある程度
ゆるめる必要があつた。 However, in this type of two-stage combustion method, one
The smaller the amount of secondary air, the greater the effect of suppressing nitrogen oxides, but the oxygen concentration in the primary combustion area decreases, the combustion temperature in that area decreases, and the mixing of fuel and air deteriorates, resulting in worsening of combustion. Since there are constraints from the combustion perspective, such as an increase in unburned matter and a significant increase in soot and dust, it was necessary to loosen the nitrogen oxide suppression effect to some extent.
また、従来の2段燃焼法では、前述の燃焼面か
らの制約上2次空気吹込み位置を十分1次燃焼炎
から遠ざけることができないために、2次空気の
干渉によつて1次燃焼域での還元雰囲気が不十分
となり、従つて前述のFuel NOxの十分な抑制効
果を期待し難いが、たとえ1次燃焼炎から2次空
気吹込み位置を十分遠ざけることができ1次燃焼
域での還元雰囲気が十分であつてFuel NOxの十
分な抑制効果があつても、前述のCombastiom
NOxに対する考慮がないために、2次燃焼域で
発生する窒素酸化物抑制が十分でなく、極低
NOx化には不十分であつた。 In addition, in the conventional two-stage combustion method, due to the aforementioned combustion constraints, it is not possible to place the secondary air injection position sufficiently far from the primary combustion flame. However, even if the secondary air injection position can be moved sufficiently far from the primary combustion flame, Even if the reducing atmosphere is sufficient and has a sufficient fuel NOx suppression effect, the Combastiom described above
Because there is no consideration for NOx, nitrogen oxides generated in the secondary combustion zone are not sufficiently suppressed, resulting in extremely low levels of nitrogen oxides.
This was insufficient for NOx conversion.
このため燃焼悪化に対しては燃焼室を大きくす
るとか、またばいじんに対しては集じん器を取付
けるなどの処置がとられてはいるが、従来の燃焼
器に単に2段目空気孔を設けているだけの部分的
改造を施しているに過ぎない。 For this reason, measures have been taken to prevent deterioration of combustion, such as enlarging the combustion chamber and installing dust collectors to prevent soot and dust, but conventional combustors are simply equipped with second-stage air holes. It has only been partially remodeled.
このように従来の2段燃焼法では、これまでの
窒素酸化物抑制の緊急対策の社会的要請から、あ
る程度の燃焼悪化、効率低下は避けられなかつた
のが実情である。しかるに、消費エネルギーの節
約の重要性は多言を要しないところで熱効率の向
上も更に一層重要な課題となつている。 As described above, in the conventional two-stage combustion method, due to the social demand for emergency measures to suppress nitrogen oxides, a certain degree of deterioration in combustion and a decrease in efficiency cannot be avoided. However, while the importance of saving energy consumption cannot be overstated, improving thermal efficiency has also become an even more important issue.
本発明によれば、従来の2段燃焼法における前
記欠点を改善し、最も理想的な2段燃焼が行なわ
れる耐火材類で構成された還元室を介装したガス
化燃焼装置が提供され、窒素酸化物を著しく低減
させるとともにばいじんも抑止でき、燃焼効率を
通常の燃焼法に比べ悪化させることもなく、か
つ、高負荷燃焼をも可能にしたものである。 According to the present invention, there is provided a gasification combustion apparatus equipped with a reduction chamber made of refractory materials that improves the drawbacks of the conventional two-stage combustion method and performs the most ideal two-stage combustion. This method significantly reduces nitrogen oxides, suppresses soot and dust, does not deteriorate combustion efficiency compared to normal combustion methods, and also enables high-load combustion.
すなわち、燃料と理論空気量以下の1次空気も
しくは1次空気と不活性ガス(燃焼ガスを含む)
の混合気体により1次燃焼を通常のバーナにおい
ても空気不足でも十分燃焼温度が上げられる耐火
材でおおわれた公知の高負荷燃焼器の予燃焼室で
行なうことにより燃料と空気の接触混合を良好な
状態に保つことができるうえ、耐火材よりなる予
燃焼室の内壁面からの幅射放熱により燃焼温度を
上げ、空気不足による未燃焼料のガス化が行なわ
れ、予燃焼室内に形成される1次燃焼域での燃焼
面の制約がなくなることから、従来法により更に
1次空気量を減らすために、酸素濃度の低下によ
り窒素酸化物の生成量が減少する。 In other words, fuel and primary air below the stoichiometric air amount, or primary air and inert gas (including combustion gas).
Good catalytic mixing of fuel and air is achieved by performing the primary combustion using a mixed gas in the pre-combustion chamber of a known high-load combustor covered with a refractory material that can raise the combustion temperature sufficiently even in a normal burner or in the absence of air. In addition, the combustion temperature is raised by radiant heat radiation from the inner wall of the pre-combustion chamber made of refractory material, and unburned fuel due to lack of air is gasified. Since there are no constraints on the combustion surface in the secondary combustion zone, the amount of nitrogen oxides produced is reduced by lowering the oxygen concentration in order to further reduce the amount of primary air using the conventional method.
また、この発明によると1次燃焼域の後方に設
けた耐火材などで構成された還元室により1次燃
焼域で生じたThermal NOx、Fuel NOxとアン
モニア(NH3)、シアン(CN)2などの中間生成物
の窒素分子N2への還元により2次燃焼域におけ
る窒素酸化物の抑制を可能とする。 In addition, according to this invention, Thermal NOx, Fuel NOx, ammonia (NH 3 ), cyanide (CN) 2, etc. generated in the primary combustion area are reduced by a reduction chamber made of refractory material installed behind the primary combustion area . The reduction of intermediate products into nitrogen molecules N2 makes it possible to suppress nitrogen oxides in the secondary combustion zone.
又、2次燃焼域における燃料の完全燃焼に対し
ては、本発明の耐火材類で構成された還元室を介
装したガス化燃焼装置の還元室の2次空気口附近
にミキシング機構を設ければ、より完全燃焼が図
られ、ばいじんも著しく低下する。 In addition, for complete combustion of the fuel in the secondary combustion zone, a mixing mechanism is provided near the secondary air port of the reduction chamber of the gasification combustion device in which the reduction chamber made of the refractory material of the present invention is interposed. This will result in more complete combustion and significantly reduce soot and dust.
以下付図に示す実施例により本発明を説明す
る。 The present invention will be explained below with reference to examples shown in the accompanying drawings.
第1図において、理論空気量以下の1次空気ま
たは1次空気と不活性ガス(燃焼ガスも含む)の
混合気体はダクト4よりウインドボツクスBに流
入し、旋回羽根8、1次空気口5を通つて凹曲面
の耐火材Aで形成された予燃焼室7に供給され
る。一方、燃料は、バーナ1より予燃焼室7内に
噴霧され、前記1次空気等と混合して燃焼を行な
いバーナ1に取付けられた保炎器2により保炎さ
れ1次燃焼炎8となる。予燃焼室7の内部の1次
燃焼において空気不足のために生じた未燃燃料
を、1次燃焼によつて生じた燃焼ガスの1部を予
燃焼室内壁の凹曲面に沿つて燃料噴射方向と反対
方向に矢示のごとく流れる反転燃焼ガス流8′の
1次空気口5への巻込みによる気体および燃料の
混合促進と予熱および予燃焼室7を形成する耐火
材Aの幅射放熱によりガス化する。 In FIG. 1, primary air below the theoretical air amount or a mixture of primary air and inert gas (including combustion gas) flows into the wind box B from the duct 4, passes through the swirl vane 8, and the primary air port 5. It is supplied to a pre-combustion chamber 7 formed of refractory material A with a concave curved surface. On the other hand, fuel is sprayed from the burner 1 into the pre-combustion chamber 7, mixed with the primary air, etc., and combusted.The flame is stabilized by the flame stabilizer 2 attached to the burner 1, and becomes a primary combustion flame 8. . Unburnt fuel produced due to lack of air during the primary combustion inside the pre-combustion chamber 7 is transferred to a part of the combustion gas produced by the primary combustion along the concave curved surface of the inner wall of the pre-combustion chamber in the fuel injection direction. The inverted combustion gas flow 8' flowing in the opposite direction as shown by the arrow is drawn into the primary air port 5 to promote the mixing of gas and fuel and preheat, and the radiant heat radiation of the refractory material A forming the pre-combustion chamber 7 Gasify.
予燃焼室7でガス化された燃料を含む燃焼ガス
10は予燃焼室の後部周壁を絞つて狭めたガス流
出口7′より耐火材9で構成された還元室Cで窒
素酸化物の還元と放熱によつて冷却され、還元室
出口9′に設けた、たとえばオリフイスの様なミ
キシング機構すなわちミキシング機能を有する構
造物11により還元室Cの後流部周壁に設けた2
次空気口6を経て供給された2次空気または2次
空気と不活性ガス(燃焼ガスも含む)の混合気体
との混合を促進されて、主燃焼室Dで燃焼を完結
する。 The combustion gas 10 containing the gasified fuel in the pre-combustion chamber 7 is passed through a gas outlet 7' narrowed by constricting the rear circumferential wall of the pre-combustion chamber to a reduction chamber C made of a refractory material 9, where nitrogen oxides are reduced. A mixing mechanism such as an orifice, ie, a structure 11 having a mixing function, is provided at the outlet 9' of the reduction chamber, and a structure 11 is provided at the downstream peripheral wall of the reduction chamber C.
The secondary air supplied through the secondary air port 6 or the mixed gas of the secondary air and the inert gas (including combustion gas) is promoted to complete combustion in the main combustion chamber D.
また、前記ミキシング機構としては、オリフイ
ス方式のほかに種々の方式が考えられる。すなわ
ち、第2図の1に示す障壁板14,2および3に
示すオリフイス障壁板11,12および11,1
3、4および5に示す2次空気旋回吹込み方式な
どの例が最も実際的で有効性に富んでいるが、そ
の他の適宜のミキシング手段によつてもかまわな
い。 Further, as the mixing mechanism, various types other than the orifice type can be considered. That is, orifice barrier plates 11, 12 and 11,1 shown in barrier plates 14, 2 and 3 shown in FIG.
Examples such as the secondary air swirl blowing method shown in 3, 4, and 5 are the most practical and effective, but other suitable mixing means may also be used.
本発明を実施する場合、耐火材類としては耐火
煉瓦を使用してもよい。 When practicing the present invention, firebricks may be used as the refractory material.
以上の説明で明らかなように、本発明によれ
ば、予燃焼室と主燃焼室の間に耐火材類で構成さ
れた還元室を設けると共に還元室後流部周壁に2
次空気口を設けたから、この還元室で1次燃焼域
での窒素酸化物の還元促進が発揮され、その後流
の前記主燃焼室で完全燃焼を行ない窒素酸化物の
発生を抑制できるので、窒素酸化物とばいじんを
大巾に低減することができる。 As is clear from the above description, according to the present invention, a reduction chamber made of refractory material is provided between the pre-combustion chamber and the main combustion chamber, and two
Since the secondary air port is provided, this reduction chamber promotes the reduction of nitrogen oxides in the primary combustion zone, and complete combustion occurs in the main combustion chamber downstream of it, suppressing the generation of nitrogen oxides. Oxides and dust can be significantly reduced.
第1図はこの発明の一実施例を示す横断面図、
第2図はミキシング機構の具体例を示す説明図で
ある。
1はバーナ、2は保炎器、3は旋回羽根、4は
1次空気ダクト、5は1次空気口、6は2次空気
口、7は予燃焼室、8は1次燃焼炎、8′は反転
燃焼ガス、9は耐火材、9′は還元室出口、10
はガス化未燃焼料、11,12,13,14,1
6はミキシング機構、Aは耐火材、Bはウインド
ボツクス、Cは還元室、Dは主燃焼室。
FIG. 1 is a cross-sectional view showing an embodiment of the present invention;
FIG. 2 is an explanatory diagram showing a specific example of the mixing mechanism. 1 is a burner, 2 is a flame stabilizer, 3 is a swirl vane, 4 is a primary air duct, 5 is a primary air port, 6 is a secondary air port, 7 is a pre-combustion chamber, 8 is a primary combustion flame, 8 ' is the inverted combustion gas, 9 is the refractory material, 9' is the reduction chamber outlet, 10
is gasified unburnt material, 11, 12, 13, 14, 1
6 is the mixing mechanism, A is the refractory material, B is the wind box, C is the reduction chamber, and D is the main combustion chamber.
Claims (1)
下の1次空気または1次空気と不活性ガス(焼燃
ガスを含む)の混合気体の雰囲気で燃焼させ、1
次燃焼を行なう後部周壁を絞つた上流の予燃焼室
と主燃焼室の間に耐火材類で構成された還元室を
設けると共に、還元室後流部周壁に2次空気口を
設けたことを特徴とする耐火材類で構成された還
元室を介装したガス化燃焼装置。1. In a two-stage fuel combustion device, combustion is performed in an atmosphere of primary air or a mixed gas of primary air and inert gas (including combustion gas) below the stoichiometric air amount, and 1.
A reduction chamber made of refractory material is provided between the upstream pre-combustion chamber and the main combustion chamber where the rear peripheral wall for subsequent combustion is narrowed, and a secondary air port is provided on the downstream peripheral wall of the reduction chamber. A gasification combustion device with a reduction chamber made of refractory materials.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP485282A JPS5840410A (en) | 1982-01-18 | 1982-01-18 | Gasification/combustion device with reducing chamber having non-cooled heat conductive plane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP485282A JPS5840410A (en) | 1982-01-18 | 1982-01-18 | Gasification/combustion device with reducing chamber having non-cooled heat conductive plane |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50036452A Division JPS587884B2 (en) | 1975-03-26 | 1975-03-26 | Gasification combustion method and its equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5840410A JPS5840410A (en) | 1983-03-09 |
| JPS6231247B2 true JPS6231247B2 (en) | 1987-07-07 |
Family
ID=11595201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP485282A Granted JPS5840410A (en) | 1982-01-18 | 1982-01-18 | Gasification/combustion device with reducing chamber having non-cooled heat conductive plane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5840410A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6149909A (en) * | 1984-08-15 | 1986-03-12 | Hideyuki Ogasawara | Low nox type high combustion chamber load burner |
| JPS61147005A (en) * | 1984-12-20 | 1986-07-04 | Matsushita Electric Ind Co Ltd | Burning equipment |
| JPS62276308A (en) * | 1986-05-22 | 1987-12-01 | Rozai Kogyo Kaisha Ltd | 2-stage combustion type nox burner |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1274637A (en) * | 1969-03-27 | 1972-05-17 | Zink Co John | Process for disposal of oxides of nitrogen |
-
1982
- 1982-01-18 JP JP485282A patent/JPS5840410A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5840410A (en) | 1983-03-09 |
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