JPH06137518A - Liquid fuel burner - Google Patents

Liquid fuel burner

Info

Publication number
JPH06137518A
JPH06137518A JP31277392A JP31277392A JPH06137518A JP H06137518 A JPH06137518 A JP H06137518A JP 31277392 A JP31277392 A JP 31277392A JP 31277392 A JP31277392 A JP 31277392A JP H06137518 A JPH06137518 A JP H06137518A
Authority
JP
Japan
Prior art keywords
fuel
temperature
vaporized
mixed fuel
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.)
Pending
Application number
JP31277392A
Other languages
Japanese (ja)
Inventor
Shuji Kameyama
修司 亀山
Kosaku Shirode
浩作 城出
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Noritz Corp
Original Assignee
Noritz Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Noritz Corp filed Critical Noritz Corp
Priority to JP31277392A priority Critical patent/JPH06137518A/en
Publication of JPH06137518A publication Critical patent/JPH06137518A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To perform clean burning by atomizing and supplying liquid fuel, evaporating and vaporizing it to burn it. CONSTITUTION:High concentration vaporized mixture fuel obtained by an evaporating chamber 42 mostly becomes dilute vaporized mixture fuel of a suitable temperature with temperature and concentration regulating air, and is partly fed to a burning unit 47 while it remains high concentration and vaporized mixture fuel. Since burning in the unit 47 is conducted mostly in dilute mixture fuel having not high temperature, a temperature of a flame is low, and discharge quantities of CO, NOx are suppressed. Since the mixture fuel fed to the unit 47 together with the dilute mixture fuel has sufficiently stable burning range for blowing of flame and back fire, the mixture fuel is burned together and hence stable burning range for the blowing of the entire flame and back fire is increased. Thus, clean burning can be conducted.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、灯油等の液体燃料を微
粒化して供給し、これを蒸発気化して燃焼に供するよう
にした液体燃料燃焼装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid fuel combustion apparatus in which a liquid fuel such as kerosene is atomized and supplied, and is vaporized to be used for combustion.

【0002】[0002]

【従来の技術】従来のこの種液体燃料燃焼装置の例を図
7、図8に沿って説明する。図7は従来装置の縦断面正
面図、図8は従来装置の縦断面側面図である。円筒状の
蒸発容器1内に蒸発室2が構成されており、液体燃料の
噴出ノズル3が円筒状蒸発容器1の中心軸上を内部の蒸
発室2へ臨まされている。液体燃料は噴出ノズル3に送
られ、蒸発室2へ微粒化状態で導入される。蒸発容器1
には前記噴出ノズル3の噴出口とは対向する端面近くの
円筒壁面に、接線方向に1個の高温空気導入口7が設け
られており、該導入口7から導入された高温空気によっ
て、蒸発室2内へ噴霧された液体燃料が比較的低い温度
で直接的に気化される。得られた気化混合燃料は同じく
円筒壁面に接線方向に設けられた送出口8から燃焼部9
へ送られ、燃焼に供される。
2. Description of the Related Art An example of a conventional liquid fuel combustion apparatus of this type will be described with reference to FIGS. FIG. 7 is a vertical sectional front view of the conventional apparatus, and FIG. 8 is a vertical sectional side view of the conventional apparatus. An evaporation chamber 2 is formed in the cylindrical evaporation container 1, and a jet nozzle 3 of the liquid fuel is exposed to the internal evaporation chamber 2 on the central axis of the cylindrical evaporation container 1. The liquid fuel is sent to the ejection nozzle 3 and introduced into the evaporation chamber 2 in the atomized state. Evaporation container 1
Is provided with one hot air inlet 7 in the tangential direction on the cylindrical wall surface near the end face facing the jet outlet of the jet nozzle 3, and the hot air introduced from the inlet 7 evaporates the hot air. The liquid fuel sprayed into the chamber 2 is directly vaporized at a relatively low temperature. The vaporized mixed fuel thus obtained is discharged from the delivery port 8 also provided in the tangential direction on the cylindrical wall surface to the combustion section 9
Sent to and used for combustion.

【0003】[0003]

【発明が解決しようとする課題】ところが上記した従来
装置においては、円筒上蒸発容器1内の限られた空間内
で、且つ限られた時間内で液体燃料の蒸発を行うことに
なるので、特に多量の燃料を蒸発気化させて高濃度の気
化混合燃料を得る場合には、前記高温空気導入口7から
導入させる高温空気の温度も一層高温にする必要が生
じ、このため、比較的低温で蒸発気化させられたはずの
気化混合燃料の温度が300 ℃を越える場合が生じる問題
があった。この気化混合燃料温度の上昇は火炎温度の上
昇を引き起こし、CO、NOX 濃度を増加させる。そこで、
出願人は、本出願と同日の特許出願において、前記蒸発
室で得られる高濃度の気化混合燃料に対して、温度調整
用の空気を混合することで、気化混合燃料の温度を適当
な温度(100 ℃〜250 ℃)に調整してCO、NOX の発生を
低減すると共に希薄な気化混合燃料として、これによっ
てもNOX の発生を低減するようにした装置を提供した。
しかしながら、燃焼に供される気化混合燃料が希薄であ
る場合には、安定燃焼範囲が狭く、火炎の吹き飛びや逆
火が生じやすいという欠点があった。
However, in the above-mentioned conventional apparatus, since the liquid fuel is vaporized within the limited space inside the cylindrical evaporation container 1 and within the limited time, When evaporating a large amount of fuel to obtain a high-concentration vaporized mixed fuel, it is necessary to raise the temperature of the high temperature air introduced from the high temperature air inlet 7 to a higher temperature. There was a problem that the temperature of the vaporized mixed fuel that had been vaporized may exceed 300 ° C. This rise in vaporized mixed fuel temperature causes rise in flame temperature and increases CO and NO X concentrations. Therefore,
In the patent application filed on the same day as the present application, the applicant mixes the temperature-adjusting air with the high-concentration vaporized-mixed fuel obtained in the vaporization chamber to adjust the temperature of the vaporized-mixed fuel to an appropriate temperature ( A device was provided which was adjusted to 100 ℃ to 250 ℃) to reduce the generation of CO and NO X , and as a lean vaporized mixed fuel, which also reduced the generation of NO X.
However, when the vaporized mixed fuel used for combustion is lean, the stable combustion range is narrow and there is a drawback that flame blow-off or flashback is likely to occur.

【0004】そこで本発明は、上記従来技術の欠点を解
消し、CO、NOX 濃度の低いクリーンな燃焼を行うことが
でき、しかも安定燃焼範囲の広い液体燃料燃焼装置の提
供を目的とする。
Therefore, an object of the present invention is to provide a liquid fuel combustion apparatus which solves the above-mentioned drawbacks of the prior art and can perform clean combustion with a low concentration of CO and NO X and has a wide stable combustion range.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明の液体燃料燃焼装置は、微粒化された液体燃
料を蒸発室内で高温空気により直接的に接触、蒸発させ
て高濃度の気化混合燃料を得ると共に、該高濃度気化混
合燃料に対してその大部分に温度及び濃度調節用の空気
を混合して希薄気化混合燃料とし且つ残りをそのまま高
濃度気化混合燃料として、両者を燃焼部に送って燃焼に
供するよう構成したことを特徴としている。
In order to achieve the above object, the liquid fuel combustion apparatus of the present invention has a high concentration of vaporized liquid fuel that is directly contacted and vaporized by hot air in the vaporization chamber. Along with obtaining the mixed fuel, most of the high-concentration vaporized mixed fuel is mixed with air for temperature and concentration adjustment to form a lean vaporized mixed fuel, and the rest is directly used as the high-concentration vaporized mixed fuel, and both are burned together. It is characterized in that it is configured so as to be sent to and used for combustion.

【0006】[0006]

【作用】上記本発明の特徴によれば、蒸発室で得られた
高濃度気化混合燃料は、大部分が温度及び濃度調節用空
気によって適当な温度の希薄気化混合燃料となり、一部
が高濃度気化混合燃料のまま燃焼部に送られる。燃焼部
での燃焼は大部分が温度の高くない希薄混合燃料である
ので、火炎の温度も低く、CO、NOX の排出量が抑えられ
る。また希薄気化混合燃料と一緒に燃焼部に送られた高
濃度気化混合燃料は火炎の吹き飛び及び逆火に対する十
分な安定燃焼幅を有することから、高濃度気化混合燃料
が一緒に燃焼することで、火炎全体としての吹き飛び、
逆火に対する安定燃焼幅が増加する。
According to the features of the present invention described above, most of the high-concentration vaporized mixed fuel obtained in the evaporation chamber becomes a lean vaporized mixed fuel at an appropriate temperature by the temperature and concentration adjusting air, and a part of the high-concentration vaporized mixed fuel The vaporized mixed fuel is sent to the combustion section as it is. Most of the combustion in the combustion section is a lean mixed fuel that is not high in temperature, so the temperature of the flame is low and the CO and NO X emissions are suppressed. In addition, since the high-concentration vaporized mixed fuel sent to the combustion section together with the lean vaporized mixed fuel has a stable combustion width that is sufficient for flame blow-off and flashback, the high-concentration vaporized mixed fuel burns together, Blown off as a whole flame,
The stable combustion width against flashback increases.

【0007】[0007]

【実施例】以下に本発明を図面に示す実施例に基づいて
説明する。図1は本発明の実施例を示す液体燃料燃焼装
置の縦断面正面図、図2は同じく本発明の実施例を示す
液体燃料燃焼装置の縦断面側面図、図3は燃焼部の詳細
を示す断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on the embodiments shown in the drawings. 1 is a vertical sectional front view of a liquid fuel combustion apparatus showing an embodiment of the present invention, FIG. 2 is a vertical sectional side view of a liquid fuel combustion apparatus similarly showing an embodiment of the present invention, and FIG. 3 shows the details of a combustion section. FIG.

【0008】蒸発容器41内に蒸発室42が構成されてお
り、液体燃料の噴出ノズル43が蒸発容器41の中心軸付近
を内部の蒸発室42へ臨まされている。液体燃料は噴出ノ
ズル43に送られ、蒸発室42へ微粒化状態で導入される。
蒸発容器41には前記噴出ノズル43の噴出口とは対向する
端面近くの円筒壁面に、接線方向に1個の高温空気導入
口45が設けられており、該導入口45から導入された高温
空気によって、蒸発室42内へ噴霧された液体燃料が直接
的に接触せられて、比較的低い温度で蒸発、気化され
る。このとき、噴霧液体燃料の量を多くし、それに伴っ
て接触蒸発させるための前記高温空気の温度を高くする
ことで、高濃度で温度の高い(例えば250 ℃から300 ℃
程度の温度となり、この温度は高温空気による直接的な
接触気化の方法の範疇において高温であるが、他の気化
方法に比べると低温であるといえる。)気化混合燃料が
得られる。得られた気化混合燃料は同じく円筒壁面に接
線方向に設けられた送出口46から導入通路54を通って燃
焼部47に送られ、燃焼に供される。前記高温空気導入口
45には空気加熱器49によって加熱された空気が高温空気
導入路48を通って供給される。高温空気導入口45と空気
が高温空気導入路48と空気加熱器49とで高温空気導入手
段をなす。
An evaporation chamber 42 is formed in the evaporation container 41, and a jet nozzle 43 of the liquid fuel faces the evaporation chamber 42 inside in the vicinity of the central axis of the evaporation container 41. The liquid fuel is sent to the jet nozzle 43 and introduced into the evaporation chamber 42 in the atomized state.
The evaporation container 41 is provided with one hot air inlet port 45 in the tangential direction on the cylindrical wall surface near the end face facing the jet port of the jet nozzle 43, and the hot air introduced from the inlet port 45 is provided. As a result, the liquid fuel sprayed into the evaporation chamber 42 is brought into direct contact with the liquid fuel, and is evaporated and vaporized at a relatively low temperature. At this time, by increasing the amount of the atomized liquid fuel and thereby increasing the temperature of the high temperature air for contact vaporization, a high concentration and high temperature (for example, 250 ℃ to 300 ℃) can be obtained.
The temperature is about the same, and this temperature is high in the category of the method of direct contact vaporization with hot air, but it can be said that it is lower than other vaporization methods. ) A vaporized mixed fuel is obtained. The vaporized mixed fuel thus obtained is sent from the delivery port 46, which is also provided tangentially to the cylindrical wall surface, to the combustion section 47 through the introduction passage 54 and is used for combustion. The hot air inlet
The air heated by the air heater 49 is supplied to 45 through the hot air introduction path 48. The high temperature air introducing port 45 and the air together with the high temperature air introducing passage 48 and the air heater 49 form high temperature air introducing means.

【0009】前記導入通路54はその途中から仕切り53に
よって大通路54aと小通路54bとに区分され、大通路54
aの途中に温度及び濃度調整用の空気混入口50が設けら
れており、空気供給装置51によって吹き出された空気が
空気通路52を通って前記空気混入口50から大通路54aに
吹き出されるようになされている。この空気混入口50と
空気供給装置51と空気通路52とで温度及び濃度調節用空
気混合手段を構成する。前記蒸発室42から導入通路54に
入った気化混合燃料はその大部分が大通路54a側に流
れ、前記空気混入口50からの空気によって適当な温度
(100 ℃〜200 ℃程度)に冷却されると共に希釈され、
太い矢印で示す希釈気化混合燃料となって燃焼部47に送
られる。残りの気化混合燃料は小通路54bを流れて、温
度調節及び希釈されることなく燃焼部47に送られる。
The introduction passage 54 is divided into a large passage 54a and a small passage 54b by a partition 53 from the middle of the introduction passage 54.
An air mixing port 50 for adjusting temperature and concentration is provided in the middle of a so that the air blown by the air supply device 51 passes through the air passage 52 and is blown from the air mixing port 50 to the large passage 54a. Has been done. The air mixing port 50, the air supply device 51, and the air passage 52 constitute temperature and concentration adjusting air mixing means. Most of the vaporized mixed fuel that has entered the introduction passage 54 from the evaporation chamber 42 flows to the large passage 54a side, and is cooled to an appropriate temperature (about 100 to 200 ° C.) by the air from the air mixing port 50. Diluted with
The diluted vaporized mixed fuel indicated by the thick arrow is sent to the combustion section 47. The remaining vaporized mixed fuel flows through the small passage 54b and is sent to the combustion section 47 without being temperature-controlled and diluted.

【0010】前記燃焼部47には、図3に示すように、主
炎孔部と補助炎孔部からなる炎孔部47aが設けられてお
り、主炎孔部への通路47bに対して前記大通路54aが接
続し、補助炎孔部への通路47cに対して前記小通路54b
が接続されている。よって炎孔部47aの主炎孔において
は大部分を占める希薄気化混合燃料が低CO、低NOX で燃
焼され、補助炎孔では残りの高濃度気化混合燃料が主炎
孔での燃焼の不安定化を防止する形で燃焼されることに
なる。
As shown in FIG. 3, the combustion section 47 is provided with a flame hole portion 47a composed of a main flame hole portion and an auxiliary flame hole portion, and the above-mentioned passage 47b to the main flame hole portion is provided with the flame hole portion 47a. The large passage 54a is connected, and the small passage 54b is connected to the passage 47c to the auxiliary flame hole portion.
Are connected. Therefore, in the main fire hole of the fire hole portion 47a lean vaporized mixed fuel occupying most is burned at a low CO, low NO X, the auxiliary flame holes remaining high concentration vaporized mixed fuel of the combustion in the main burner ports not It will be burned in a manner that prevents stabilization.

【0011】図4は、燃焼部及び該燃焼部への導入通路
に関する変形実施例を示す断面図である。この例では、
導入通路54の途中からを仕切り管55で二重管状にし、仕
切り管55内を大通路54aとし、周囲を小通路54bとし
て、燃焼部57の炎孔部57aの主炎孔への通路57bに大通
路54aを接続し、燃焼部57の炎孔部57aの補助炎孔への
通路57cに小通路54bを接続している。小通路54bを通
った高濃度気化混合燃料は燃焼部57内の周囲から補助炎
孔用通路57cへ送られる。
FIG. 4 is a sectional view showing a modification of the combustion section and the introduction passage to the combustion section. In this example,
A partition pipe 55 is formed in a double tube form from the middle of the introduction passage 54, a large passage 54a is formed inside the partition pipe 55, and a small passage 54b is formed around the inside of the introduction pipe 54. The large passage 54a is connected, and the small passage 54b is connected to the passage 57c to the auxiliary flame hole of the flame hole portion 57a of the combustion portion 57. The high-concentration vaporized mixed fuel that has passed through the small passage 54b is sent to the auxiliary flame hole passage 57c from the inside of the combustion section 57.

【0012】図5、図6に他の実施例を示す。図5は他
の実施例を示す液体燃料燃焼装置の縦断面図、図6は図
5のC−C断面図である。気化燃料(ガス燃料または液
体燃料を気化したもの)を噴出する噴出ノズル61が燃焼
部67の混合燃料入口62に臨まされており、噴出ノズル61
から噴出された燃料は空気と混合されながら高濃度混合
燃料となって燃焼部67内の第1混合室65に入る。この第
1混合室65は両側の仕切り壁63を介して第2混合室66と
隣合い、この仕切り壁63には分配孔64が設けられてい
る。この分配孔64から高濃度混合燃料の少しが第2混合
室66に流れ込む。分配孔64のある位置よりも下流側の第
1混合室65に対して空気導入口70が開口しており、図示
しない空気供給装置からの空気が第1混合室65に吹き込
まれることによって高濃度混合燃料が希釈された混合燃
料とされる。この希釈混合燃料は第1混合室65から炎孔
部67aの中央に続く吹き出し室68に導かれて、炎孔部67
aの中央で主炎として燃焼せられる。前記第2混合室66
に入った高濃度混合燃料はそのまま炎孔部67aの両側で
補助炎として燃焼せられる。
5 and 6 show another embodiment. FIG. 5 is a vertical sectional view of a liquid fuel combustion apparatus showing another embodiment, and FIG. 6 is a sectional view taken along line CC of FIG. A jet nozzle 61 for jetting vaporized fuel (gas fuel or liquid fuel vaporized) faces the mixed fuel inlet 62 of the combustion section 67.
The fuel ejected from the mixture becomes high-concentration mixed fuel while being mixed with air, and enters the first mixing chamber 65 in the combustion section 67. The first mixing chamber 65 is adjacent to the second mixing chamber 66 via the partition walls 63 on both sides, and the partition wall 63 is provided with a distribution hole 64. A small amount of the high-concentration mixed fuel flows into the second mixing chamber 66 from the distribution hole 64. The air introduction port 70 is opened to the first mixing chamber 65 on the downstream side of the position where the distribution hole 64 is provided, and the air from the air supply device (not shown) is blown into the first mixing chamber 65, so that the high concentration is achieved. The mixed fuel is a diluted mixed fuel. The diluted mixed fuel is guided from the first mixing chamber 65 to the blowing chamber 68 continuing to the center of the flame hole portion 67a, and the flame hole portion 67a.
It is burned as the main flame in the center of a. The second mixing chamber 66
The high-concentration mixed fuel that has entered is burned as an auxiliary flame on both sides of the flame hole 67a as it is.

【0013】[0013]

【発明の効果】本発明は以上の構成よりなり、請求項1
に記載の液体燃料燃焼装置によれば、微粒化された液体
燃料を蒸発室内で高温空気により直接的に接触、蒸発さ
せて高濃度の気化混合燃料を得ると共に、該高濃度気化
混合燃料に対してその大部分に温度及び濃度調節用の空
気を混合して希薄気化混合燃料とし且つ残りをそのまま
高濃度気化混合燃料として、両者を燃焼部に送って燃焼
に供するよう構成したので、燃焼部での大部分の燃焼は
温度の高くない希薄混合燃料による燃焼であるので、C
O、NOX の排出量の少ないクリーンな燃焼を達成するこ
とができる。しかも高濃度気化混合燃料が燃焼部で一緒
に燃焼することで良好な補助炎となり、火炎全体として
の吹き飛び、逆火に対する安定燃焼幅を増加することが
できる。
According to the present invention, which has the above-described structure,
According to the liquid fuel combustion apparatus described in (1), the atomized liquid fuel is directly contacted and evaporated by high temperature air in the evaporation chamber to obtain a high concentration vaporized mixed fuel, and the high concentration vaporized mixed fuel is Since most of the air is mixed with temperature and concentration adjusting air to form a lean vaporized mixed fuel and the rest as a high concentration vaporized mixed fuel, both are sent to the combustion section for combustion, so that the combustion section Since most of the combustion is due to the lean mixed fuel that does not have high temperature,
It is possible to achieve clean combustion with low emissions of O and NO X. In addition, the high-concentration vaporized mixed fuel burns together in the combustion section to form a good auxiliary flame, and it is possible to increase the stable combustion width against blowout and flashback as the entire flame.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例を示す液体燃料燃焼装置の縦断
面正面図である。
FIG. 1 is a vertical sectional front view of a liquid fuel combustion apparatus showing an embodiment of the present invention.

【図2】本発明の実施例を示す液体燃料燃焼装置の縦断
面側面図である。
FIG. 2 is a vertical sectional side view of a liquid fuel combustion apparatus showing an embodiment of the present invention.

【図3】燃焼部の詳細を示す断面図である。FIG. 3 is a cross-sectional view showing details of a combustion section.

【図4】燃焼部及び該燃焼部への導入通路に関する変形
実施例を示す断面図である。
FIG. 4 is a cross-sectional view showing a modified example relating to a combustion section and an introduction passage to the combustion section.

【図5】他の実施例を示す液体燃料燃焼装置の縦断面図
である。
FIG. 5 is a vertical cross-sectional view of a liquid fuel combustion apparatus showing another embodiment.

【図6】図5のC−C断面図である。6 is a cross-sectional view taken along line CC of FIG.

【図7】従来装置の縦断面正面図である。FIG. 7 is a vertical cross-sectional front view of a conventional device.

【図8】従来装置の縦断面側面図である。FIG. 8 is a vertical sectional side view of a conventional device.

【符号の説明】[Explanation of symbols]

41 蒸発容器 42 蒸発室 43 噴出ノズル 45 高温空気導入口 46 送出口 47、57 燃焼部 50 空気混入口 53 仕切り 54 導入通路 54a 大通路 54b 小通路 55 仕切り管 41 Evaporation container 42 Evaporation chamber 43 Jet nozzle 45 High temperature air inlet 46 Outlet 47, 57 Combustion section 50 Air mixing port 53 Partition 54 Inlet passage 54a Large passage 54b Small passage 55 Partition pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 微粒化された液体燃料を蒸発室内で高温
空気により直接的に接触、蒸発させて高濃度の気化混合
燃料を得ると共に、該高濃度気化混合燃料に対してその
大部分に温度及び濃度調節用の空気を混合して希薄気化
混合燃料とし且つ残りをそのまま高濃度気化混合燃料と
して、両者を燃焼部に送って燃焼に供するよう構成した
ことを特徴とする液体燃料燃焼装置。
1. A highly concentrated vaporized mixed fuel is obtained by directly contacting and vaporizing atomized liquid fuel with high temperature air in an evaporation chamber, and most of the highly concentrated vaporized mixed fuel is temperature-controlled. And a concentration-adjusting air to form a lean vaporized mixed fuel, and the rest as a high-concentration vaporized mixed fuel, both of which are sent to a combustion section for combustion.
JP31277392A 1992-10-27 1992-10-27 Liquid fuel burner Pending JPH06137518A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31277392A JPH06137518A (en) 1992-10-27 1992-10-27 Liquid fuel burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31277392A JPH06137518A (en) 1992-10-27 1992-10-27 Liquid fuel burner

Publications (1)

Publication Number Publication Date
JPH06137518A true JPH06137518A (en) 1994-05-17

Family

ID=18033244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31277392A Pending JPH06137518A (en) 1992-10-27 1992-10-27 Liquid fuel burner

Country Status (1)

Country Link
JP (1) JPH06137518A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010110147A1 (en) * 2009-03-27 2010-09-30 新日本石油株式会社 Kerosene carburetor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010110147A1 (en) * 2009-03-27 2010-09-30 新日本石油株式会社 Kerosene carburetor

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