JPH11294722A - Oxygen burner - Google Patents
Oxygen burnerInfo
- Publication number
- JPH11294722A JPH11294722A JP10122910A JP12291098A JPH11294722A JP H11294722 A JPH11294722 A JP H11294722A JP 10122910 A JP10122910 A JP 10122910A JP 12291098 A JP12291098 A JP 12291098A JP H11294722 A JPH11294722 A JP H11294722A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- nozzle
- fuel
- air
- concentration
- 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.)
- Withdrawn
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/10—Reduction of greenhouse gas [GHG] emissions
- Y02P10/143—Reduction of greenhouse gas [GHG] emissions of methane [CH4]
Landscapes
- Pre-Mixing And Non-Premixing Gas Burner (AREA)
- Spray-Type Burners (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、酸素バーナの低NOx
化に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low NOx oxygen burner.
It is about the conversion.
【0002】[0002]
【従来の技術】図4は従来の酸素バーナの構造を示した
もので、燃焼空気の代わりに純酸素又は高濃度酸素(以
下高酸素ガスという)を使用するものである。図7
(a)は酸素バーナにおける酸素濃度と火炎温度との関
係を示したものであるが、一般に酸素濃度が高くなるほ
ど火炎温度も高くなるため、高温や急速加熱が必要な溶
解炉等に、それぞれ必要とされる火炎温度に応じて、適
当な酸素濃度の高濃度酸素が使用されている。またこの
グラフからも明らかなように、酸素濃度が高くなるにつ
れて火炎温度が飽和する傾向にあり、例えば酸素濃度6
0%前後で使用すれば比較的火炎温度が高く、しかも酸
素使用量も節減できて効率がよいので、通常は図5に示
すように、高酸素ガスに空気を混合して所望の酸素濃度
として使用している。2. Description of the Related Art FIG. 4 shows the structure of a conventional oxygen burner in which pure oxygen or high-concentration oxygen (hereinafter referred to as high oxygen gas) is used instead of combustion air. FIG.
(A) shows the relationship between the oxygen concentration in the oxygen burner and the flame temperature. Generally, the higher the oxygen concentration, the higher the flame temperature. High-concentration oxygen having an appropriate oxygen concentration is used depending on the flame temperature. Also, as is clear from this graph, the flame temperature tends to be saturated as the oxygen concentration increases, and for example, the oxygen concentration is 6%.
When used at around 0%, the flame temperature is relatively high, the amount of oxygen used can be reduced, and the efficiency is high. Therefore, usually, as shown in FIG. 5, air is mixed with high oxygen gas to obtain a desired oxygen concentration. I'm using
【0003】[0003]
【発明が解決しようとする課題】しかし上述のような従
来構成においては、次に述べるような問題があった。図
7(b)の曲線Aは、図4あるいは図5の酸素バーナを
用いた場合の燃焼空気中の酸素濃度と排気中のNOx濃
度との関係を測定したものであるが、このグラフを見る
と酸素濃度60%付近でNOx濃度が最も高くなってい
る。すなわちNOx発生量は、窒素ガスの豊富なときに
は温度の増加と共に増加するが、窒素ガスが少なくなっ
てくると、今度は窒素濃度に比例して減少する傾向にあ
り、従って図5のように、酸素バーナに供給する高酸素
ガスに適量の空気を混合して、酸素バーナの燃料コスト
を節約しようとすると、排ガス中のNOx発生量が増加
してしまうという問題があった。However, the above-described conventional configuration has the following problems. Curve A in FIG. 7 (b) is obtained by measuring the relationship between the oxygen concentration in the combustion air and the NOx concentration in the exhaust when the oxygen burner in FIG. 4 or 5 is used. The NOx concentration is highest around 60% oxygen concentration. That is, when the amount of nitrogen gas is abundant, the amount of NOx increases with an increase in the temperature, but when the amount of nitrogen gas decreases, the amount of NOx tends to decrease in proportion to the nitrogen concentration. Therefore, as shown in FIG. If an appropriate amount of air is mixed with the high oxygen gas supplied to the oxygen burner to reduce the fuel cost of the oxygen burner, the amount of NOx generated in the exhaust gas increases.
【0004】図6は、低NOx化の手法として知られて
いる空気二段燃焼方式を、上述のように酸素量を節約し
て運転される酸素バーナに適用したものであり、図7
(b)の曲線Bは図6の酸素バーナによるNOx濃度を
測定したものである。この方式によれば、一段目で酸素
不足となり燃焼が緩慢になるので、若干のNOx低減効
果が認められるものの、到底満足できるものではなかっ
た。そこで本発明は上述のような問題点を解消し、酸素
使用量を節約した場合に問題となるNOx濃度を低く抑
えることができるような、この種の酸素バーナを提供す
ることを目的とするものである。FIG. 6 shows an application of a two-stage air combustion system known as a method for reducing NOx to an oxygen burner operated with a reduced amount of oxygen as described above.
Curve B in (b) is obtained by measuring the NOx concentration by the oxygen burner in FIG. According to this method, the first stage causes a shortage of oxygen and slows combustion, so that although a slight NOx reduction effect is recognized, it was not completely satisfactory. Therefore, an object of the present invention is to provide an oxygen burner of this type which can solve the above-mentioned problems and can suppress the NOx concentration which becomes a problem when the oxygen consumption is reduced. It is.
【0005】[0005]
【課題を解決するための手段】本発明による酸素バーナ
は、図1(a)あるいは(b)に示すように、燃料を噴
出する燃料ノズル1の周囲に、高酸素ガス(純酸素又は
高濃度酸素)を噴出する酸素ノズル2を備え、更にその
外側に空気ノズル3を備えたものであり、あるいは図2
に示すように、燃料ノズル1の周囲に空気ノズル3を備
え、更にその外側に高酸素ガスを噴出する酸素ノズル2
を備えたものであって、火炎中に酸素濃度が高い比較的
高温の部分と、酸素濃度が低くて窒素濃度が高く従って
比較的低温の部分とを作ることにより、窒素成分をでき
るだけ高温域に接触させないようにして、NOx発生量
を抑制した点に特徴を有するものである。As shown in FIG. 1 (a) or (b), an oxygen burner according to the present invention has a high oxygen gas (pure oxygen or high concentration) around a fuel nozzle 1 for ejecting fuel. An oxygen nozzle 2 for ejecting oxygen) and an air nozzle 3 on the outside thereof, or FIG.
As shown in FIG. 1, an air nozzle 3 is provided around a fuel nozzle 1 and an oxygen nozzle 2 for jetting high oxygen gas outside the air nozzle 3.
By making a relatively high temperature part with high oxygen concentration in the flame and a relatively low temperature part with low oxygen concentration and high nitrogen concentration in the flame, the nitrogen component is kept as high as possible in the flame. The feature is that the amount of NOx generated is suppressed by preventing the contact.
【0006】[0006]
【発明の実施の形態】図1(a)は本発明による酸素バ
ーナの一実施例を示したもので、燃料としては天然ガ
ス、プロパンガス等の気体燃料を使用してもよく、重
油、灯油等の液体燃料を使用してもよい。燃料を噴出す
る燃料ノズル1は、高酸素ガスすなわち純酸素又は高濃
度酸素が供給される酸素ノズル2の中心部に設けられて
おり、酸素ノズル2の外側に等角度間隔で複数の空気ノ
ズル3が列設されている。図3は本発明によるNOx低
減効果を従来例と比較して示したもので、曲線Cは図1
の実施例による測定結果を示したものであり、曲線A及
びBは図7(b)の従来例を再掲したものである。また
図1(b)は本発明の他の実施例を示したもので、火炎
をバーナの外部に形成するようにして燃料ノズル1の耐
久性を向上したものであるが、低NOx効果については
図1(a)の場合とほとんど変わらない。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1A shows an embodiment of an oxygen burner according to the present invention. As the fuel, a gaseous fuel such as natural gas or propane gas may be used. Or other liquid fuels. A fuel nozzle 1 for ejecting fuel is provided at a central portion of an oxygen nozzle 2 to which high oxygen gas, that is, pure oxygen or high concentration oxygen is supplied, and a plurality of air nozzles 3 at equal angular intervals outside the oxygen nozzle 2. Are lined up. FIG. 3 shows the NOx reduction effect of the present invention in comparison with the conventional example.
7A and 7B show the measurement results according to the embodiment of the present invention, and curves A and B are again obtained by reprinting the conventional example shown in FIG. 7B. FIG. 1 (b) shows another embodiment of the present invention, in which a flame is formed outside the burner to improve the durability of the fuel nozzle 1. This is almost the same as the case of FIG.
【0007】図2は本発明の他の実施例を示したもの
で、燃料ノズル1の周囲に空気ノズル3を備え、更にそ
の外側に複数の酸素ノズル2を列設したものであり、こ
れによるNOx低減効果を図3の曲線Dに示す。この場
合にも、図1の場合と同様、高酸素ガスと燃焼空気とは
予混合せずに別個に噴射させている。この方式において
も高温燃焼を行う高酸素ガス中では窒素濃度が低くなる
ので、NOx発生率は従来例よりは低下するものの、周
囲の空気が高温部に接触するために、図1の構成による
低NOx効果には及ばない。しかし図1における燃料ノ
ズル1や燃焼筒の内壁の温度上昇を抑えることができる
ので、バーナの耐久性が向上するという利点がある。FIG. 2 shows another embodiment of the present invention, in which an air nozzle 3 is provided around a fuel nozzle 1 and a plurality of oxygen nozzles 2 are further arranged outside the air nozzle 3. The NOx reduction effect is shown by curve D in FIG. Also in this case, similarly to the case of FIG. 1, the high oxygen gas and the combustion air are separately injected without premixing. Also in this method, the nitrogen concentration becomes lower in the high oxygen gas which performs high-temperature combustion, so that the NOx generation rate is lower than that of the conventional example. It does not reach the NOx effect. However, since the temperature rise of the fuel nozzle 1 and the inner wall of the combustion cylinder in FIG. 1 can be suppressed, there is an advantage that the durability of the burner is improved.
【0008】[0008]
【発明の効果】本発明によれば上述のように、酸素に空
気を混合して燃料コストを節減する方式の酸素バーナに
おいて、コスト節約のために生じるNOx発生の問題
を、きわめて簡単な構成によって解消し得るという利点
があり、また予め酸素と空気とを混合せずにバーナに供
給するものであるから、図5のような混合器5を必要と
しない上に、従来保安上の理由から排熱で高酸素ガスを
予熱できないという問題があったが、本方式では空気を
予熱することができるという利点がある。According to the present invention, as described above, in an oxygen burner of the type in which air is mixed with oxygen to reduce fuel costs, the problem of NOx generation occurring for cost saving can be solved by a very simple structure. It has the advantage that it can be eliminated, and because it is supplied to the burner without mixing oxygen and air in advance, it does not require the mixer 5 as shown in FIG. Although there was a problem that high oxygen gas could not be preheated by heat, this method has an advantage that air can be preheated.
【図1】本発明の一実施例を示すもので、(a)は縦断
面図、(b)は正面図。FIG. 1 shows an embodiment of the present invention, in which (a) is a longitudinal sectional view and (b) is a front view.
【図2】本発明の他の実施例を示すもので、(a)は縦
断面図、(b)は正面図。FIG. 2 shows another embodiment of the present invention, wherein (a) is a longitudinal sectional view and (b) is a front view.
【図3】本発明の効果を示すグラフ。FIG. 3 is a graph showing the effect of the present invention.
【図4】従来例を示す縦断面図。FIG. 4 is a longitudinal sectional view showing a conventional example.
【図5】他の従来例を示す縦断面図。FIG. 5 is a longitudinal sectional view showing another conventional example.
【図6】更に他の従来例を示すもので、(a)は縦断面
図、(b)は正面図。6A and 6B show still another conventional example, in which FIG. 6A is a longitudinal sectional view, and FIG. 6B is a front view.
【図7】(a)及び(b)は酸素バーナの動作を示すグ
ラフ。FIGS. 7A and 7B are graphs showing the operation of an oxygen burner.
1 燃料ノズル 2 酸素ノズル 3 空気ノズル 4 バーナ本体 5 混合器 DESCRIPTION OF SYMBOLS 1 Fuel nozzle 2 Oxygen nozzle 3 Air nozzle 4 Burner body 5 Mixer
Claims (3)
あるいは重油、灯油等の液体燃料を噴出する燃料ノズル
の周囲に純酸素又は高濃度酸素を噴出する酸素ノズルを
備え、更にその外側に空気ノズルを備えて成る酸素バー
ナ。1. A gaseous fuel such as natural gas or propane gas;
Alternatively, an oxygen burner including an oxygen nozzle for ejecting pure oxygen or high-concentration oxygen around a fuel nozzle for ejecting liquid fuel such as heavy oil or kerosene, and further including an air nozzle on the outside thereof.
あるいは重油、灯油等の液体燃料を噴出する燃料ノズル
の周囲に空気ノズルを備え、更にその外側に純酸素又は
高濃度酸素を噴出する酸素ノズルを備えて成る酸素バー
ナ。2. A gaseous fuel such as natural gas or propane gas;
Alternatively, an oxygen burner including an air nozzle around a fuel nozzle for ejecting a liquid fuel such as heavy oil or kerosene, and an oxygen nozzle for ejecting pure oxygen or high-concentration oxygen outside the fuel nozzle.
より予熱するようにして成る請求項1又は2記載の酸素
バーナ。3. The oxygen burner according to claim 1, wherein air supplied to the air nozzle is preheated by exhaust gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10122910A JPH11294722A (en) | 1998-04-16 | 1998-04-16 | Oxygen burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10122910A JPH11294722A (en) | 1998-04-16 | 1998-04-16 | Oxygen burner |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11294722A true JPH11294722A (en) | 1999-10-29 |
Family
ID=14847642
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10122910A Withdrawn JPH11294722A (en) | 1998-04-16 | 1998-04-16 | Oxygen burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11294722A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100599381B1 (en) | 2004-10-01 | 2006-07-12 | 한국에너지기술연구원 | Pure oxygen/Air combustion combined burner |
JP2006275335A (en) * | 2005-03-28 | 2006-10-12 | Osaka Gas Co Ltd | Burner for melting furnace and melting furnace |
KR100867744B1 (en) | 2008-05-26 | 2008-11-10 | 박정재 | Oxygen burner |
JP2009281615A (en) * | 2008-05-20 | 2009-12-03 | Osaka Gas Co Ltd | Combustion device for heating furnace |
JP2012078033A (en) * | 2010-10-04 | 2012-04-19 | Kinsei Sangyo:Kk | Dry distillation and gasification typed incinerator |
JP2013119488A (en) * | 2011-12-06 | 2013-06-17 | Asahi Glass Co Ltd | Burner, glass fusion furnace therewith, method of forming combustion flame, method of manufacturing molten glass and method of manufacturing glass product |
KR101481126B1 (en) * | 2012-08-16 | 2015-01-12 | 주식회사 포스코 | Apparatus for manufacturing molten iron |
WO2015064792A1 (en) * | 2013-11-01 | 2015-05-07 | 주식회사 한별 | Industrial boiler attachment-type syngas combustion device |
JP2021055970A (en) * | 2019-10-01 | 2021-04-08 | 中外炉工業株式会社 | Liquid fuel combustion apparatus |
-
1998
- 1998-04-16 JP JP10122910A patent/JPH11294722A/en not_active Withdrawn
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100599381B1 (en) | 2004-10-01 | 2006-07-12 | 한국에너지기술연구원 | Pure oxygen/Air combustion combined burner |
JP2006275335A (en) * | 2005-03-28 | 2006-10-12 | Osaka Gas Co Ltd | Burner for melting furnace and melting furnace |
JP2009281615A (en) * | 2008-05-20 | 2009-12-03 | Osaka Gas Co Ltd | Combustion device for heating furnace |
KR100867744B1 (en) | 2008-05-26 | 2008-11-10 | 박정재 | Oxygen burner |
JP2012078033A (en) * | 2010-10-04 | 2012-04-19 | Kinsei Sangyo:Kk | Dry distillation and gasification typed incinerator |
JP2013119488A (en) * | 2011-12-06 | 2013-06-17 | Asahi Glass Co Ltd | Burner, glass fusion furnace therewith, method of forming combustion flame, method of manufacturing molten glass and method of manufacturing glass product |
KR101481126B1 (en) * | 2012-08-16 | 2015-01-12 | 주식회사 포스코 | Apparatus for manufacturing molten iron |
WO2015064792A1 (en) * | 2013-11-01 | 2015-05-07 | 주식회사 한별 | Industrial boiler attachment-type syngas combustion device |
JP2021055970A (en) * | 2019-10-01 | 2021-04-08 | 中外炉工業株式会社 | Liquid fuel combustion apparatus |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20050705 |