JPS599003B2 - Method and device for suppressing nitrogen oxides - Google Patents
Method and device for suppressing nitrogen oxidesInfo
- Publication number
- JPS599003B2 JPS599003B2 JP51094937A JP9493776A JPS599003B2 JP S599003 B2 JPS599003 B2 JP S599003B2 JP 51094937 A JP51094937 A JP 51094937A JP 9493776 A JP9493776 A JP 9493776A JP S599003 B2 JPS599003 B2 JP S599003B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- heat transfer
- transfer member
- liquid
- 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.)
- Expired
Links
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title claims description 39
- 238000000034 method Methods 0.000 title claims description 6
- 239000007789 gas Substances 0.000 claims description 57
- 239000007788 liquid Substances 0.000 claims description 35
- 238000002485 combustion reaction Methods 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000010419 fine particle Substances 0.000 claims description 6
- 230000001629 suppression Effects 0.000 claims 1
- 238000002347 injection Methods 0.000 description 9
- 239000007924 injection Substances 0.000 description 9
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000002309 gasification Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000001294 propane Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 230000003685 thermal hair damage Effects 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
Landscapes
- Combustion Of Fluid Fuel (AREA)
Description
【発明の詳細な説明】
この発明はノズルプレートの内域からガス、外域から燃
焼空気をそれぞれ高速噴射する工業炉用ガスバーナーに
おいて、液体微粒子を燃焼空気と混合する前のガス噴流
中に強制混合する前に、噴水系統が炉内高温ガスの影響
を受けることなく円滑に噴射され、かつ水性ガス化反応
が行なわれるようにして燃焼時に発生する窒素酸化物を
効果的に抑制する方法および装置に関する。DETAILED DESCRIPTION OF THE INVENTION This invention is a gas burner for industrial furnaces that injects gas from the inner area of the nozzle plate and combustion air from the outer area at high speed. The present invention relates to a method and apparatus for effectively suppressing nitrogen oxides generated during combustion by ensuring that the fountain system can smoothly inject water without being affected by high-temperature gas in the furnace and that a water gasification reaction can take place. .
従来、工業炉用ガスバーナーの燃焼時に発生する窒素酸
化物の抑制手段として、加圧した水蒸気または水を通す
内管と、燃料を通す外管のそれぞれに噴出口を設ける2
重管バーナーにおいて、内管に設ける噴出口を外管に設
ける噴出口と近接して、バーナーの長手力向に対し直角
又は直角に近い角度で開口せしめてなるバーナーを、前
方固囲にバーナータイルを備えた加熱炉に装着したもの
がある(実願昭49−105266号(実開昭51−3
1834号)の願書に添付した明細書及び図面の内容を
撮影したマイクロフイルム参照)。Conventionally, as a means of suppressing nitrogen oxides generated during combustion in gas burners for industrial furnaces, jet ports are provided in each of the inner tube through which pressurized steam or water passes, and the outer tube through which fuel passes.
In a heavy pipe burner, a burner with a jet nozzle provided in the inner pipe close to a jet port provided in the outer pipe and opened at a right angle or close to a right angle to the longitudinal direction of the burner is installed in front of the burner tile. There is a device that is attached to a heating furnace equipped with
(See the microfilm photographing the contents of the specification and drawings attached to the application No. 1834).
このものは燃焼空気と混合する前のガス噴流中に液体の
微粒子を強制混合させることによって燃焼排ガス中の窒
素酸化物を除去するものであるとはいえ、バーナー自体
は加熱炉中にむき出しの状態で突出させる構造としてお
り、しかも内管の噴出口から噴出する水量は極めて微量
である結果、噴出日付近の温度が炉内高温ガスによって
700〜800℃に熱せられると、噴出口からの水は高
温高圧水蒸気になりバックプレッシャーが働らき、水が
噴出しなくなる。Although this device removes nitrogen oxides from the combustion exhaust gas by forcibly mixing liquid particles into the gas jet before mixing with the combustion air, the burner itself is exposed inside the heating furnace. Moreover, the amount of water that spews out from the spout of the inner tube is extremely small.As a result, when the temperature near the spout date is heated to 700-800℃ by the high temperature gas in the furnace, the water from the spout will The water turns into high-temperature, high-pressure steam, creating back pressure and preventing water from gushing out.
従って炉内温度が初期段階の比較的低温度下では、バー
ナーの内管から水が円滑に噴出するが、炉内が高温下で
は水の噴出機能が著しく低下し使用困難となるか、或い
はこれを解消するために多量の高圧噴水を行なう必要が
あり、微粒子の粒度も大きくなり熱効率を著しく下げた
り、又ガスとの混合により着火不良となる等窒素酸化物
抑制以前の問題が生ずること5なる。Therefore, when the temperature inside the furnace is relatively low in the initial stage, water can be smoothly jetted out from the inner pipe of the burner, but when the inside of the furnace is at high temperatures, the water jetting function is significantly reduced, making it difficult to use, or it may become difficult to use. In order to eliminate this problem, it is necessary to use a large amount of high-pressure water fountain, and the particle size of the fine particles increases, which significantly reduces thermal efficiency, and also causes problems before nitrogen oxide control, such as poor ignition due to mixing with gas. .
この発明は上記の点に鑑みてなされたものでその目的と
するところは、ノズルプレートの内域からガス、外域か
ら燃焼空気をそれぞれ高速噴射する工業炉用ガスバーナ
ーにおいて、液体微粒子を燃焼空気と混合する前のガス
噴流中に強制混合する前に、噴水系統から噴出する高速
旋回流の液体を狭窄状の噴射空気膜にて炉内高温ガスか
ら効果的に保護する一方、前記旋回流の液体を一層微粒
化すると5もに十分攪拌混合されて水性ガス化を図り、
炉内高温下においてもバックプレッシャー等が働らくこ
となく噴水系統を円滑に機能させ、燃焼時に発生する窒
素酸化物を効果的に抑制する方法及びその装置を提供す
ることにある。This invention has been made in view of the above points, and its purpose is to provide a gas burner for industrial furnaces in which gas is injected from the inner region of the nozzle plate and combustion air is injected from the outer region at high speed. Before being forcedly mixed into the gas jet before mixing, the liquid in the high-speed swirling flow spouted from the fountain system is effectively protected from the high-temperature gas in the furnace by a constricted jet air film, while the liquid in the swirling flow is When it is further atomized, it is thoroughly stirred and mixed with 5 to achieve water gasification,
It is an object of the present invention to provide a method and device for effectively suppressing nitrogen oxides generated during combustion by allowing a fountain system to function smoothly without back pressure or the like even under high temperatures inside a furnace.
以下、本発明を図面に基いて説明する。Hereinafter, the present invention will be explained based on the drawings.
図において1はノズルプレートで、その内域にはガスa
の噴射口2が、外域には燃焼空気bの噴射口3がそれぞ
れ設けられている。In the figure, 1 is a nozzle plate, inside which gas a
An injection port 2 for combustion air b is provided in the outer area, and an injection port 3 for combustion air b is provided in the outer area.
前記ガスaの噴射口2は外方に傾斜し、燃焼空気bの噴
射口3は内方に傾斜する如く設けられ、これら噴射口2
,3から噴射されたガスaおよび燃焼空気bは混合せら
れ、パイロットバーナー(図示せず)により着火するこ
とにより火焔を形成する。The injection ports 2 for the gas a are provided so as to be inclined outward, and the injection ports 3 for the combustion air b are provided to be inclined inward.
, 3 are mixed and ignited by a pilot burner (not shown) to form a flame.
4はノズルプレート1の中心部に、該プレート1と直交
する如く該プレートの内側から嵌着した管状の伝熱部材
である。Reference numeral 4 denotes a tubular heat transfer member fitted into the center of the nozzle plate 1 from the inside of the plate so as to be orthogonal to the plate.
伝熱部材4はその肉厚内の同心田上に所定間隔をおいて
軸線に沿って複数の空気通路を形成するとトもに、各対
応する空気通路と連通ずる伝熱部材4の前端面に複数の
空気噴出口4′を設ける。The heat transfer member 4 forms a plurality of air passages along the axis at predetermined intervals on concentric surfaces within its wall thickness, and a plurality of air passages are formed on the front end surface of the heat transfer member 4 communicating with each corresponding air passage. An air outlet 4' is provided.
しかして伝熱部材4の前端面に同心田上に配した複数の
空気吐出口4′からは前記燃焼空気bの一部b′が内方
に向け狭窄状に噴射して噴射空気膜を形成し、該空気膜
が後述する高速旋回流の微粒状液体を炉内高温ガスから
有効に保護しバックプレッシャーが働らかないようにす
るものである。A portion b' of the combustion air b is injected inward from a plurality of air discharge ports 4' arranged concentrically on the front end surface of the heat transfer member 4 in a narrow shape to form an injected air film. The air film effectively protects the fine liquid particles in the high-speed swirling flow, which will be described later, from the high-temperature gas in the furnace and prevents back pressure from working.
噴射空気膜は伝熱部材の空気通路を通る過程で熱せられ
、さらに炉内高温ガスにより熱せられるとはいえ、連続
的に噴射して一種のエアーカーテンの役割を果すもので
あるから炉内温度に比べはるかに低く、バックプレッシ
ャーの発生を防ぐに十分な温度域であることを要する。Although the injected air film is heated during the process of passing through the air passage of the heat transfer member and is further heated by the high-temperature gas inside the furnace, it is continuously injected and acts as a kind of air curtain, so the temperature inside the furnace does not change. The temperature range must be much lower than that of the previous one, and must be in a temperature range sufficient to prevent back pressure from occurring.
また空気吐出口4′と連通ずる空気通路の端部は前記ガ
スaの噴射口2に連通ずるガス流送管6内を縦通ずる空
気流送管7に連通する如くしている。Further, the end of the air passage communicating with the air discharge port 4' communicates with an air flow pipe 7 extending vertically within the gas flow pipe 6 communicating with the injection port 2 of the gas a.
5は伝熱部材4内に一定の環状空隙Sを残し、かつ該伝
熱部材4より凹んだ位置に先端が位置するよう同心円状
に設けた液体ノズル体である。Reference numeral 5 denotes a liquid nozzle body which is arranged concentrically so that a certain annular gap S is left in the heat transfer member 4 and its tip is located at a position recessed from the heat transfer member 4.
液体ノズル体5の先端を伝熱部材4より凹ませたのは、
炉内高温ガスの熱的影響を少なくするためである。The reason why the tip of the liquid nozzle body 5 is recessed from the heat transfer member 4 is because
This is to reduce the thermal influence of high temperature gas in the furnace.
該液体ノズル体5はその内部に液体Cを旋回させるため
のノズルピース9を設け、該ノズルピース9を通した旋
回流を微粒状に高圧噴射できる構造になっている。The liquid nozzle body 5 is provided with a nozzle piece 9 for swirling the liquid C therein, and has a structure in which the swirling flow through the nozzle piece 9 can be jetted in the form of fine particles at high pressure.
そして液体ノズル体5の先端ノズルは該ノズルから噴射
する微粒状の液体が伝熱部材先端部内壁に向けて入・反
射し、該反射後の水性ガスが前記狭窄状の噴射空気膜を
突き破って燃焼空気と混合する前のガス噴流中に強制混
合するように形成されている。The fine liquid ejected from the tip nozzle of the liquid nozzle body 5 enters and reflects toward the inner wall of the tip of the heat transfer member, and the water gas after the reflection breaks through the constricted injected air film. It is designed for forced mixing in the gas jet before mixing with the combustion air.
また前記液体ノズル体5は前記空気流送管7内を縦通ず
る液体流送管8に連通している。Further, the liquid nozzle body 5 communicates with a liquid flow pipe 8 that runs vertically within the air flow pipe 7.
この液体流送管8はその先端部に設けた環状突起8′を
介して前記伝熱部材4の後部内壁に密接し、該環状突起
8′が空気流送管7にて流送された空気の漏出を防止す
ると5もに前記環状空隙Sのスペーサーを兼ね得るよう
になっている。This liquid flow pipe 8 is in close contact with the rear inner wall of the heat transfer member 4 via an annular projection 8' provided at its tip, and the annular projection 8' allows the air flowed by the air flow pipe 7 to By preventing the leakage of the annular gap S, the ring 5 can also serve as a spacer for the annular gap S.
しかして液体ノズル体5内の液体Cはノズルピース9を
通って高速旋回し、液体ノズル体5の先端ノズルから微
粒状となって高速噴射し、該微粒状の液体が伝熱部材4
の先端部内壁に激しく当ってこ5で該微粒子をさらに一
層細かく破壊して極微細粒子(30〜50μ)となると
同時に伝熱部材4内壁からの熱を受けて高温化され、水
性ガス化することができる。Thus, the liquid C in the liquid nozzle body 5 passes through the nozzle piece 9, swirls at high speed, becomes fine particles, and is jetted at high speed from the tip nozzle of the liquid nozzle body 5, and the fine liquid C passes through the nozzle piece 9 and is jetted at high speed.
By violently hitting the inner wall of the tip of the heat transfer member 5, the fine particles are further broken down into ultrafine particles (30 to 50μ), and at the same time, they are heated to a high temperature by receiving heat from the inner wall of the heat transfer member 4, and turn into water gas. I can do it.
一方、該水性ガスはその外側周囲の空気吐出口4′から
狭窄状に噴出する噴射空気膜に覆われ炉内高温ガスから
保護されており、バックプレッシャーを発生させること
なく水性ガスが前記噴射空気膜を突き破って燃焼空気と
混合する前のガス噴流中に強制混合すること\なる。On the other hand, the water gas is protected from the high-temperature gas inside the furnace by being covered with a jet air film that jets out in a narrow shape from the air discharge port 4' around the outside, and the water gas is protected from the high-temperature gas in the furnace without generating back pressure. Forced mixing occurs in the gas jet before it breaks through the membrane and mixes with the combustion air.
この発明は上記の説明から判るように、ノズルプレート
の内域からガス、外域から燃焼空気を高速噴射する工業
炉用ガスバーナーにおいて、前記ノズルプレートの中心
部の凹んだ位置から高速旋回流の液体を、ノズルプレー
トの中心部に嵌着した管状伝熱部材の先端部内壁に向け
て入・反射する如く微流状に高圧噴射せしめ、該反射時
に微粒化液体を高温化すると同時に一層微粒化して水性
ガス化する一方、前記伝熱部材の前端面から燃焼空気の
一部を内方に向け狭窄状に噴射して前記水性ガスを炉内
高温ガスから保護し、さらに反射後の水性ガスが前記狭
窄状の噴射空気膜を突き破って燃焼空気と混合する前の
ガス噴流中に強制混合することを特徴とする窒素酸化物
の抑制方法であるから、液体微粒子を燃焼空気と混合す
る前のガス噴流中に強制混合する前段において、噴水系
統から噴出する高速旋回流の液体を狭窄状の噴射空気膜
にて炉内高温ガスから効果的に保護する一方、前記旋回
流の液体を一層微粒化するとメもに十分攪拌混合されて
水性ガス化を図り、炉内高温下においてもバックプレッ
シャー等が働らくことなく噴水系統を円滑に機能させる
ことができる。As can be seen from the above description, the present invention provides a gas burner for industrial furnaces in which gas is injected from the inner region of the nozzle plate and combustion air is injected from the outer region at high speed. is injected at high pressure in the form of fine streams so as to enter and reflect toward the inner wall of the tip of the tubular heat transfer member fitted in the center of the nozzle plate, and at the time of reflection, the temperature of the atomized liquid is raised and at the same time it is further atomized. While turning into water gas, part of the combustion air is injected inward from the front end face of the heat transfer member in a constricted shape to protect the water gas from the high temperature gas in the furnace, and furthermore, the water gas after reflection is This method of suppressing nitrogen oxides is characterized by forced mixing in the gas jet before breaking through a constricted injection air film and mixing with the combustion air. In the pre-stage where the liquid is forcibly mixed in the furnace, the liquid in the high-speed swirling flow ejected from the fountain system is effectively protected from the high-temperature gas in the furnace by a constricted jet air film, while the liquid in the swirling flow is further atomized. The water gas is sufficiently stirred and mixed to achieve water gasification, and the fountain system can function smoothly without back pressure or the like even at high temperatures inside the furnace.
また前述の如く噴水系統はバックプレッシャーを受ける
ことがないために、従来のように噴水系統から多量に水
を高圧噴射させる必要がなく微量でよい結果、燃焼空気
と混合する前のガス噴流中には微量の水性ガスを混入さ
せることかでき、熱効率を低下させることがなく、しか
も着火不良も生ぜずに合理的に燃焼時の窒素酸化物を抑
制できる。In addition, as mentioned above, since the fountain system does not receive back pressure, there is no need to inject a large amount of water at high pressure from the fountain system as in the past, and only a small amount is required. It is possible to mix in a small amount of water gas, and it is possible to rationally suppress nitrogen oxides during combustion without reducing thermal efficiency or causing ignition failure.
また、ノズルプレートの内域からガス、外域から燃焼空
気をそれぞれ高速噴射する工業炉用ガスバーナーにおい
て、前記ノズルプレートの中心部に管状の伝熱部材を嵌
着し、該伝熱部材の肉厚内の空気通路を通る燃焼空気の
一部が前方内方に向け狭窄状に噴射する如く伝熱部材の
前端面に複数の空気噴出口を設けるとともに、該伝熱部
材内に一定の環状空隙を残し、かつ該伝熱部材より凹ん
だ位置に先端が位置するよう同心円状に液体ノズル体を
設け、該液体ノズル体内に液体を旋回させるノズルピー
スを設け、さらに液体ノズル体の先端ノズルは該ノズル
から噴射する微粒状の液体が伝熱部材先端部内壁に向け
て入・反射し、該反射後の水性ガスが前記狭窄状の噴射
空気膜を突き破って燃称空気と混合する前のガス噴流中
に強制混合するように形成したことを特徴とする窒素酸
化物の抑制装置としたから、これによって上記効果を奏
する具体的手段が実現される上に、液体ノズル体の先端
が伝熱部材よりも凹んだ位置にあること5、伝熱部材前
端面の空気吐出口から狭窄状に噴射する空気噴射膜によ
って保護されること5が相俟って液体ノズル体は炉内高
温ガスによる熱的損傷を受けることなく長期使用が可能
となる。In addition, in a gas burner for an industrial furnace that injects gas from the inner region of the nozzle plate and combustion air from the outer region at high speed, a tubular heat transfer member is fitted in the center of the nozzle plate, and the wall thickness of the heat transfer member is A plurality of air jet ports are provided on the front end surface of the heat transfer member so that a part of the combustion air passing through the air passage inside is injected forward and inward in a narrow shape, and a certain annular gap is provided within the heat transfer member. A liquid nozzle body is provided concentrically so that the tip is located at a position recessed from the heat transfer member, and a nozzle piece for swirling the liquid is provided in the liquid nozzle body, and further, the tip nozzle of the liquid nozzle body Particulate liquid injected from the heat transfer member enters and reflects toward the inner wall of the tip of the heat transfer member, and the water gas after the reflection breaks through the constricted jet air film and mixes with the fuel air during the gas jet. Since the nitrogen oxide suppressing device is characterized in that it is formed so as to forcefully mix the nitrogen oxides with The liquid nozzle body is protected from thermal damage by high-temperature gas in the furnace due to its concave position5 and the fact that it is protected by an air jet film that is jetted in a constricted shape from the air discharge port on the front end face of the heat transfer member. It can be used for a long time without any damage.
実験例:
図面に示すノズルプレートを有する高速燃焼バーナー(
1 4 0,0 0 0 Kcal負荷)を用いて、
ノズルプレートの中心部から水を圧力2 kg/cya
下に84 cc/minの割合で微粒状に高速旋回流噴
射すると5もに、該プレートの内域から5, 0 0
0 Kcalのプロパンガスを、外域から燃焼空気をそ
れぞれ高速噴射し、前記プロパンガスが燃焼空気と混合
する以前に前記微粒状噴射水をプロパンガス中に強制混
合した。Experimental example: A fast combustion burner with the nozzle plate shown in the drawing (
1 4 0,0 0 0 Kcal load),
Water is pumped from the center of the nozzle plate at a pressure of 2 kg/cya.
When a high-speed swirling flow is injected downward in the form of fine particles at a rate of 84 cc/min, 5,00
0 Kcal of propane gas was injected into combustion air from an external area at high speed, and the particulate injection water was forcibly mixed into the propane gas before the propane gas was mixed with the combustion air.
この時の炉内温度における燃焼ガス中の窒素酸化物の低
減率は次の通りであった。The reduction rate of nitrogen oxides in the combustion gas at the furnace temperature at this time was as follows.
第1図はこの発明の装置の一例を示す断面図、第2図は
要部の拡大図である。
1・・・・・・ノズルプレート、2・・・・・・ガス噴
射口、3・・・・・・燃焼空気噴射口、4・・・・・・
伝熱部材、5・・・・・・ノズル体。FIG. 1 is a sectional view showing an example of the device of the present invention, and FIG. 2 is an enlarged view of the main parts. 1... Nozzle plate, 2... Gas injection port, 3... Combustion air injection port, 4...
Heat transfer member, 5... Nozzle body.
Claims (1)
を高速噴射する工業炉用ガスバーナーにおいて、前記ノ
ズルプレートの中心部の凹んだ位置から高速旋回流の液
体を、ノズルプレートの中心部に嵌着した管状伝熱部材
の先端部内壁に向けて入・反射する如く微粒状に高圧噴
射せしめ、該反射時に微粒化液体を高温化すると同時に
一層微粒化して水性ガス化する一方、前記伝熱部材の前
端面から燃焼空気の一部を内方に向けて狭窄状に噴射し
て前記水性ガスを炉内高温ガスから保護し、さらに反射
後の水性ガスが前記狭窄状の噴射空気膜を突き破って燃
焼空気と混合する前のガス噴流中に強制混合することを
特徴とする窒素酸化物の抑制方法。 2 ノズルプレートの内域からガス、外域から燃焼空気
をそれぞれ高速噴射する工業炉用ガスバーナーにおりて
、前記ノズルプレートの中心部に管状の伝熱部材を嵌着
し、該伝熱部材の肉厚内の空気通路を通る燃焼空気の一
部が前方内方に向け狭窄状に噴射する如く伝熱部材の前
端面に複数の空気出口を設けるとともに、該伝熱部材内
に一定の環状空隙を残し、かつ該伝熱部材より凹んだ位
置に先端が位置するよう同心円状に液体ノズル体を設け
、該液体ノズル体内に液体を旋回させるノズルピースを
設け、さらに液体ノズル体の先端ノズルは該ノズルから
噴射する微粒状の液体が伝熱部材先端部内壁に向けて入
・反射し、該反射後の水性ガスが前記狭窄状の噴射空気
膜を突き破って燃焼空気と混合する前のガス噴流中に強
制混合するように形成したことを特徴とする窒素酸化物
の抑制装置。[Claims] 1. In a gas burner for an industrial furnace that injects gas from the inner region of the nozzle plate and combustion air from the outer region at high speed, a liquid in a high-speed swirling flow is injected from a concave position in the center of the nozzle plate to the nozzle plate. The liquid is jetted at high pressure in the form of fine particles so as to enter and reflect toward the inner wall of the tip of the tubular heat transfer member fitted in the center of the tube, and at the time of reflection, the temperature of the atomized liquid is increased, and at the same time, it is further atomized and turned into a water gas. , a part of the combustion air is injected inward from the front end surface of the heat transfer member in a constricted shape to protect the water gas from the high temperature gas in the furnace, and furthermore, the water gas after reflection is injected in the constricted shape. A method for suppressing nitrogen oxides characterized by forced mixing in a gas jet before breaking through an air film and mixing with combustion air. 2. In an industrial furnace gas burner that injects gas from the inner region of the nozzle plate and combustion air from the outer region at high speed, a tubular heat transfer member is fitted in the center of the nozzle plate, and the heat transfer member is heated. A plurality of air outlets are provided on the front end surface of the heat transfer member so that a part of the combustion air passing through the air passage within the thickness is injected forward and inward in a narrow shape, and a certain annular gap is provided within the heat transfer member. A liquid nozzle body is provided concentrically so that the tip is located at a position recessed from the heat transfer member, and a nozzle piece for swirling the liquid is provided in the liquid nozzle body, and further, the tip nozzle of the liquid nozzle body The fine particulate liquid injected from the heat transfer member enters and reflects toward the inner wall of the tip of the heat transfer member, and the water gas after the reflection breaks through the constricted jet air film and mixes with the combustion air in the gas jet. A nitrogen oxide suppression device characterized in that it is formed so as to perform forced mixing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51094937A JPS599003B2 (en) | 1976-08-11 | 1976-08-11 | Method and device for suppressing nitrogen oxides |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51094937A JPS599003B2 (en) | 1976-08-11 | 1976-08-11 | Method and device for suppressing nitrogen oxides |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5321431A JPS5321431A (en) | 1978-02-27 |
| JPS599003B2 true JPS599003B2 (en) | 1984-02-28 |
Family
ID=14123857
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51094937A Expired JPS599003B2 (en) | 1976-08-11 | 1976-08-11 | Method and device for suppressing nitrogen oxides |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS599003B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60122304U (en) * | 1984-01-28 | 1985-08-17 | 高尾 美智子 | Disposable sweat absorbing collar |
| JPS63158901U (en) * | 1987-04-08 | 1988-10-18 |
-
1976
- 1976-08-11 JP JP51094937A patent/JPS599003B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60122304U (en) * | 1984-01-28 | 1985-08-17 | 高尾 美智子 | Disposable sweat absorbing collar |
| JPS63158901U (en) * | 1987-04-08 | 1988-10-18 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5321431A (en) | 1978-02-27 |
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