JPS5892703A - Combustion apparatus - Google Patents
Combustion apparatusInfo
- Publication number
- JPS5892703A JPS5892703A JP56191634A JP19163481A JPS5892703A JP S5892703 A JPS5892703 A JP S5892703A JP 56191634 A JP56191634 A JP 56191634A JP 19163481 A JP19163481 A JP 19163481A JP S5892703 A JPS5892703 A JP S5892703A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- gas
- primary combustion
- inner cylinder
- combustion chamber
- 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
- F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
- F23C3/002—Combustion apparatus characterised by the shape of the combustion chamber the chamber having an elongated tubular form, e.g. for a radiant tube
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
Description
【発明の詳細な説明】 この発明は燃焼装置に関する。[Detailed description of the invention] This invention relates to a combustion device.
一般に熱処理炉等に用いら九るラジアントチューブは、
チューブの端部にバーナを設け、チューブ内で燃料を燃
焼させて得た高温の燃焼ガヌによりチューブを加熱する
形式のものであるので、上記バーナの火焔の高温部にお
いてN0x(窒素酸化物)が発生しやすい。そこで低N
Ox化バーナの一種である二段燃焼形バーナの採用が試
みられm−。Radiant tubes generally used in heat treatment furnaces, etc.
A burner is installed at the end of the tube, and the tube is heated by the high-temperature combustion gas obtained by burning fuel within the tube, so NOx (nitrogen oxides) are generated in the high temperature part of the flame of the burner. is likely to occur. So low N
Attempts were made to adopt a two-stage combustion burner, which is a type of oxidizing burner.
でいる。このバーナは一次燃焼室において空気量を理論
必要空気量より少なくして燃料の一次燃焼をおこない、
得られた一次燃焼ガスに二次燃焼室において不足分の空
気量を供給して二次燃焼させ完全燃焼させるものである
。これにより最高火炎温度を低下させてNOxの生成の
抑制をはかるものであるが、充分な低Nqx化の達成は
困難であった。I'm here. This burner performs primary combustion of fuel by reducing the amount of air in the primary combustion chamber than the theoretically required amount of air,
The resulting primary combustion gas is supplied with the insufficient amount of air in the secondary combustion chamber to cause secondary combustion and complete combustion. Although this is intended to reduce the maximum flame temperature and suppress the generation of NOx, it has been difficult to achieve a sufficient reduction in Nqx.
この発明は上記の点にかんがみてなされたもので、大巾
な低NOx化が達成できる燃焼装置を提供しようとする
ものである。This invention has been made in view of the above points, and is intended to provide a combustion device that can achieve a significant reduction in NOx.
以上第1図および第2図によりこの発明の詳細な説明す
る。The present invention will be described in detail with reference to FIGS. 1 and 2.
図中、lは加熱炉の加熱室、2は炉壁で、3はこの炉壁
を貫通して取付けたラジアントチューブ、4はその本体
であるところの耐熱鋳鋼製のチューブである。5は燃料
導管、6は内筒で、いずれもチューブ4内に該チューブ
と同心状に配設されている。内筒6は金属やセラミック
等の耐熱材料を網状、ハニカム状、せんい伏、多孔質状
などの通気性を有する形状に成形して適宜厚さの円筒状
としたものであり、該内筒を通過するガスと接触する実
質的な表面積が充分大きいもので1.ある。内筒6はチ
ューブ4の加熱室l内部分、すなわち被熱物加熱面に対
応する位置に設けてあり、7は内筒6の先端部とチュー
ブ4との間に設けたシールリング、8は内筒6とチュー
ブ4との間に形成した環状の一次燃焼室である。また9
は内筒6内と燃料導管5内とを仕切る隔壁、IOは燃料
導管5の端部周壁に複数個穿設した燃料噴出孔、11は
燃料導管5内に連通ずる燃料供給管、12は燃料流入口
で、図示しない燃料ガス供給源に接続されている。また
13は一次燃焼室8への一次空気流入口である。14は
内筒dより排ガスロ倶1のチューブ4内に形成した二次
燃焼室で、内筒6内に連通している。15は二次空気供
給管で、チューブ4の端壁および隔壁9を一通して設け
られ、先端は一次燃焼室84に向って開口しており、1
6はその二次空気流入口である。In the figure, 1 is a heating chamber of a heating furnace, 2 is a furnace wall, 3 is a radiant tube that is attached through the furnace wall, and 4 is a tube made of heat-resistant cast steel, which is the main body. Reference numeral 5 indicates a fuel conduit, and reference numeral 6 indicates an inner cylinder, both of which are disposed within the tube 4 concentrically with the tube. The inner cylinder 6 is made of a heat-resistant material such as metal or ceramic and formed into a cylindrical shape with an appropriate thickness by molding a heat-resistant material such as a mesh, honeycomb, perforated, or porous shape. 1. The substantial surface area in contact with the passing gas is sufficiently large. be. The inner cylinder 6 is provided in the inside of the heating chamber 1 of the tube 4, that is, at a position corresponding to the heating surface of the object to be heated, 7 is a seal ring provided between the tip of the inner cylinder 6 and the tube 4, and 8 is a seal ring. This is an annular primary combustion chamber formed between the inner cylinder 6 and the tube 4. Also 9
1 is a partition wall that partitions the inside of the inner cylinder 6 and the inside of the fuel conduit 5, IO is a plurality of fuel injection holes bored in the peripheral wall at the end of the fuel conduit 5, 11 is a fuel supply pipe communicating with the inside of the fuel conduit 5, and 12 is a fuel The inlet is connected to a fuel gas supply source (not shown). Further, 13 is a primary air inlet into the primary combustion chamber 8. A secondary combustion chamber 14 is formed in the tube 4 of the exhaust gas flow 1 from the inner cylinder d, and communicates with the inner cylinder 6. A secondary air supply pipe 15 is provided through the end wall of the tube 4 and the partition wall 9, and its tip is open toward the primary combustion chamber 84.
6 is the secondary air inlet.
上記構成の装置において、燃料ガスを燃料流入口12に
、燃焼用−次空気および二次空気を各空気流入口13お
よび16にそれぞれ供給し、−次空気と燃料噴出孔10
より流出する燃料ガスとの混合気に図示しない点火装置
により点火すれば、先ず一次燃焼室8におい゛て理論必
要空気量以下の一次空気により燃料ガスが一次燃焼(不
完全燃焼)する。得られた一次燃焼ガスは第1図゛中に
矢印Xで示すように一次燃焼室8内から内筒6の壁面を
通過して内筒6内に流入するが、このとき実質的表面積
が大きい内筒6は対流熱伝達により一次燃焼ガスの湿層
に近い高温に効率よく加熱され、−次燃焼ガスは内筒6
からチューブ4への熱放射により顕熱を奪われて低温と
なって内筒6内を経て二次燃焼室14内へ流入する。こ
のため−次燃焼ガスの高温域滞留時間の短縮により一次
燃焼におけるNOxの発生が抑制されるとともに、二次
空気供給管15よりの二次空気により二次燃焼する際の
燃焼y7n度が低くなるため、二次燃焼におけるNOx
の発生量も少ない。一方高温となった内筒6は固体であ
るためガスよりはるかに大きなふく射射出能力を有する
ので、チューブ4に大量のふく射熱を放射して該チュー
ブを直接昇温させる。In the apparatus configured as described above, fuel gas is supplied to the fuel inlet 12, secondary air for combustion and secondary air are supplied to the respective air inlets 13 and 16, and the secondary air and the fuel nozzle 10 are supplied.
When the mixture with the fuel gas flowing out is ignited by an ignition device (not shown), the fuel gas undergoes primary combustion (incomplete combustion) in the primary combustion chamber 8 using primary air that is less than the theoretically required air amount. The obtained primary combustion gas flows from the primary combustion chamber 8 through the wall surface of the inner cylinder 6 and into the inner cylinder 6 as shown by the arrow X in FIG. The inner cylinder 6 is efficiently heated to a high temperature close to the wet layer of the primary combustion gas by convection heat transfer, and the secondary combustion gas is heated to a high temperature close to the wet layer of the primary combustion gas.
Sensible heat is removed by heat radiation from the tube 4 to the tube 4, the temperature becomes low, and the temperature flows into the secondary combustion chamber 14 through the inner cylinder 6. Therefore, by shortening the residence time of the secondary combustion gas in the high temperature region, the generation of NOx in the primary combustion is suppressed, and the combustion temperature during secondary combustion is lowered by the secondary air from the secondary air supply pipe 15. Therefore, NOx in secondary combustion
The amount of generation is also small. On the other hand, since the heated inner cylinder 6 is a solid and has a much greater radiation emitting capacity than a gas, it radiates a large amount of radiation heat to the tube 4 and directly raises the temperature of the tube.
さ゛らに内筒6のふく射熱により該円筒の壁面内を通過
する一次燃焼ガス中の未燃分がほぼ均一に加熱され、二
次燃焼における酸素過剰率を低くしても完全燃焼がおこ
なわれるため、二次燃焼におけるNOx発生量は一層抑
制されるのである。Furthermore, the unburned content in the primary combustion gas passing through the wall of the cylinder is heated almost uniformly by the radiant heat of the inner cylinder 6, and complete combustion can be achieved even if the excess oxygen ratio in the secondary combustion is low. The amount of NOx generated during secondary combustion is further suppressed.
以上のように通気性を有する内筒6による一次燃焼ガス
の顕熱のふく射熱への変換作用により、主として一次燃
焼ガスの低温化による低NOx化がはかられるが、この
内筒6の内面部および/または外面部あるいは内筒6全
体にNOx還元触媒として作用する白金やパラジウムな
どの活性成分を担持させて内筒6にNOx還元触媒層を
形成させれば、−次燃焼によって生成したNOxは内筒
6を通過する際に還元されN2ガスとなるので、全体と
してのNOx発生量をさらに低下させるこ。As described above, through the action of converting the sensible heat of the primary combustion gas into radiant heat by the air permeable inner cylinder 6, reduction in NOx is achieved mainly by lowering the temperature of the primary combustion gas, but the inner surface of the inner cylinder 6 And/or if an active component such as platinum or palladium that acts as a NOx reduction catalyst is supported on the outer surface or the entire inner cylinder 6 to form a NOx reduction catalyst layer in the inner cylinder 6, the NOx generated by the secondary combustion can be reduced. Since it is reduced to N2 gas when passing through the inner cylinder 6, the overall amount of NOx generated can be further reduced.
とができるのである。It is possible to do this.
次に上記構成のラジアントチュ−ブ(外伜178閣、炉
内中2000 twyn )を用いた発明者の実験結果
(ラジアントチューブの排ガス中のNO濃度測定値)を
第3図に示す。内筒6としてはステンレス金網(線径I
IIIll、12メツシユ)を6層積層して円筒状に成
形したものを用い、内筒6に触媒層を形成しない場合を
曲線D1、内筒6の外面に白金系金属を担持させてNO
x還元触媒層を形成した場合を曲線D2で示す。また曲
線D」は通常の二段燃焼形バーナを用いた場合を示す。Next, FIG. 3 shows the results of the inventor's experiment (measured NO concentration in the exhaust gas of the radiant tube) using the radiant tube having the above configuration (178 kaku, 2000 twins in the furnace). The inner cylinder 6 is made of stainless steel wire mesh (wire diameter I
Curve D1 is the case where a catalyst layer is not formed on the inner cylinder 6, and NO is when a platinum-based metal is supported on the outer surface of the inner cylinder 6.
The case where the x reduction catalyst layer is formed is shown by curve D2. Curve D'' shows the case where a normal two-stage combustion burner is used.
図から明−らかなように本発明による場合のNO濃度は
、たとえば炉温900℃において従来の二段燃焼形バー
ナ使用例の50〜60%と大巾に減少している。As is clear from the figure, the NO concentration in the case of the present invention is significantly reduced by 50 to 60% of that in the case of using a conventional two-stage combustion burner at a furnace temperature of 900 DEG C., for example.
以上はこの発明をラジアントチューブに適用した場合に
ついて説明したが、この発明は各種用途向バーナなどの
他の燃焼装置にも適用できるものである。またチューブ
4は耐熱鋼、セラミックス、耐火物など各種の材料で構
成することができる。Although the present invention has been described above in the case where it is applied to a radiant tube, the present invention can also be applied to other combustion devices such as burners for various uses. Further, the tube 4 can be made of various materials such as heat-resistant steel, ceramics, and refractories.
以上説明したようにこの発明によれば、チューブ内に設
けた通気性を有する内筒により一次燃焼ガスの顕熱をふ
く射熱に変換するようにしたので、−次燃焼ガスの低温
化により一次燃焼および二次燃焼の際のNOx発生量が
抑制されるとともに、チューブは内筒からあふく射伝熱
により加熱され、−次燃焼熱を効率よく放熱させてチュ
ーブの加熱に有効に利用できる。また高部の一部または
全体に還元触媒層を形成させることにより、さらに低N
Ox化をはかることができる。As explained above, according to the present invention, the sensible heat of the primary combustion gas is converted into radiant heat by the air permeable inner cylinder provided in the tube, so that the primary combustion and The amount of NOx generated during secondary combustion is suppressed, and the tube is heated by radiation heat transfer from the inner cylinder, and secondary combustion heat can be efficiently radiated and effectively used to heat the tube. In addition, by forming a reduction catalyst layer on part or all of the high part, even lower N
Oxification can be achieved.
第1図はこの発明の一実施例を示すラジアントチューブ
の部分縦断面図、第2図は同じくラジアントチューブの
排ガス中のNO濃度線図である。
3・・・ラジアントチューブ、4・・・チューブ、5・
・・燃料導管、6・・・内筒、8・・・−次燃焼室、1
0・・・燃料噴出孔、11・・・燃料供給管、14・・
・二次燃焼室、15・・・二次空気供給管。
出願人 大同特殊鋼株式会社
代理人 乾 凸 雄FIG. 1 is a partial vertical cross-sectional view of a radiant tube showing an embodiment of the present invention, and FIG. 2 is a NO concentration diagram in exhaust gas of the radiant tube. 3...Radiant tube, 4...Tube, 5...
... Fuel conduit, 6... Inner cylinder, 8... Secondary combustion chamber, 1
0... Fuel injection hole, 11... Fuel supply pipe, 14...
- Secondary combustion chamber, 15... secondary air supply pipe. Applicant: Daido Steel Co., Ltd. Agent: Yu Inui
Claims (1)
記チューブと上記内筒との間に環状の一次燃焼室を形成
させ、上記−次燃焼室に燃料および一次空気を供給する
燃料供給路および一次空気供給路を設け、上記内筒より
排ガス口側の上記チューブ内空間を二次燃焼寥として該
二次燃焼室を上記円筒内に連通させ、上記二次燃焼室内
に二次空気を供給する二次空気供給路を設けて成る燃焼
装置。 2、 チューブ内に通気性を有する内筒を設けて、上記
チューブと上記内筒との間に環状の一次燃焼室を形成さ
せ、上記−次燃焼室に燃料および一次空気を供給する燃
料供給路および一次空気供給路を設け、上記内筒よシ排
ガスロ側の上記チューブ内空間を二次燃焼室として該二
次燃焼室を上記内筒内に連通させ、上記二次燃焼室内に
二次空気を供給する二次空気供給路を設けるとともに、
上記内筒にNOx還元触媒層を形成して成る燃焼装置。[Claims] 1. A cylinder having ventilation is provided in the tube, an annular primary combustion chamber is formed between the tube and the inner cylinder, and fuel and primary air are supplied to the secondary combustion chamber. A fuel supply path and a primary air supply path are provided for supplying the air, and the space inside the tube on the exhaust gas port side from the inner cylinder is used as a secondary combustion chamber, and the secondary combustion chamber is communicated with the inside of the cylinder. A combustion device comprising a secondary air supply path for supplying secondary air to the combustion equipment. 2. A fuel supply path for supplying fuel and primary air to the secondary combustion chamber by providing an inner cylinder with ventilation inside the tube to form an annular primary combustion chamber between the tube and the inner cylinder. and a primary air supply passage is provided, the space within the tube on the exhaust gas outlet side of the inner cylinder is used as a secondary combustion chamber, and the secondary combustion chamber is communicated with the inner cylinder, and secondary air is supplied into the secondary combustion chamber. In addition to providing a secondary air supply path that supplies
A combustion device comprising a NOx reduction catalyst layer formed in the inner cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56191634A JPS5892703A (en) | 1981-11-28 | 1981-11-28 | Combustion apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56191634A JPS5892703A (en) | 1981-11-28 | 1981-11-28 | Combustion apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5892703A true JPS5892703A (en) | 1983-06-02 |
JPS6260605B2 JPS6260605B2 (en) | 1987-12-17 |
Family
ID=16277911
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56191634A Granted JPS5892703A (en) | 1981-11-28 | 1981-11-28 | Combustion apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5892703A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6150630A (en) * | 1984-07-11 | 1986-03-12 | ロ−ヌ−プ−ラン シミ− ドウ バ−ズ | Gas contacting method and apparatus |
JPS62197135A (en) * | 1986-01-02 | 1987-08-31 | ロ−ヌ−プ−ラン・シミ・ド・バ−ズ | Method and apparatus for forming gaseous substance at high temperature |
KR100466178B1 (en) * | 2001-12-21 | 2005-01-13 | 주식회사 포스코 | A low NOx regenerative radiant tube burner equipped with multiple fuel nozzles |
WO2017212744A1 (en) * | 2016-06-07 | 2017-12-14 | 中外炉工業株式会社 | Radiant tube burner unit, and industrial furnace |
-
1981
- 1981-11-28 JP JP56191634A patent/JPS5892703A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6150630A (en) * | 1984-07-11 | 1986-03-12 | ロ−ヌ−プ−ラン シミ− ドウ バ−ズ | Gas contacting method and apparatus |
JPS62197135A (en) * | 1986-01-02 | 1987-08-31 | ロ−ヌ−プ−ラン・シミ・ド・バ−ズ | Method and apparatus for forming gaseous substance at high temperature |
KR100466178B1 (en) * | 2001-12-21 | 2005-01-13 | 주식회사 포스코 | A low NOx regenerative radiant tube burner equipped with multiple fuel nozzles |
WO2017212744A1 (en) * | 2016-06-07 | 2017-12-14 | 中外炉工業株式会社 | Radiant tube burner unit, and industrial furnace |
Also Published As
Publication number | Publication date |
---|---|
JPS6260605B2 (en) | 1987-12-17 |
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