JPS60200012A - Liquid fuel burner - Google Patents

Liquid fuel burner

Info

Publication number
JPS60200012A
JPS60200012A JP5470684A JP5470684A JPS60200012A JP S60200012 A JPS60200012 A JP S60200012A JP 5470684 A JP5470684 A JP 5470684A JP 5470684 A JP5470684 A JP 5470684A JP S60200012 A JPS60200012 A JP S60200012A
Authority
JP
Japan
Prior art keywords
fuel
vaporization
combustion
combustion air
evaporation surface
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
JP5470684A
Other languages
Japanese (ja)
Inventor
Yasushi Hirata
康 平田
Katsuhiko Yamamoto
克彦 山本
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP5470684A priority Critical patent/JPS60200012A/en
Publication of JPS60200012A publication Critical patent/JPS60200012A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/005Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space with combinations of different spraying or vaporising means

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Spray-Type Burners (AREA)

Abstract

PURPOSE:To control accumulation of tar on an evaporation surface, by a method wherein fuel is evaporated while it is being turned, and a position where the fuel collides directly against the evaporation surface is shifted in the direction of turning than a position where combustion air collides directly against the evaporation surface. CONSTITUTION:Fuel is injected along with combustion air along the inner circumference of an evaporation chamber 1 from a blast pipe 4, evaporated on an evaporation surface 7 provided on an inner wall of evaporation chamber 1 while it is being turned and supplied to a combustion part 8 of the upper part for combustion while it is being mixed. In this instance, a position where the fuel collides directly against the evaporation surface 7, that is, a collision surface 9 of the fuel is kept shifted slightly in the direction of turning than a position where the combustion air collides directly against the evaporation surface 7, that is, a collision surface 10 of the air. With this construction, a partial cooling phenomenon of the evaporation surface through the fuel and the combustion air is mitigated, generation and accumulation of tar are almost eliminated and generation of a foul odor at the time of ignition, extinction and combustion and carbon monoxide are decreased.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は家庭用の暖房器等に応用化される石油を燃料と
した気化予混合燃焼の燃焼装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a combustion device for vaporization premix combustion using petroleum as fuel, which is applied to household heaters and the like.

従来例のFA−成とその問題点 従来のこの種の液体燃料燃焼装置は第1図に示すように
471□成されている。すなわち円筒有底状の気化室1
の腹面部円周方向に加熱用ヒータ2を装設し、開放面に
絞り形状を有する混合板3を装イニ1している。さらに
気化室1の一部に送風管4を接合して、これより気化室
1内に燃焼空気を送風ファン5より送るとともに、燃料
ノズル6を送風管4中を通して気化室1内にのそませて
いる。燃料は燃焼空気とともに気化室1の内壁に設けら
れた気化面7で気化され、混合されながら」一部の燃焼
部8に供給され、燃焼する。
Conventional FA Construction and Its Problems A conventional liquid fuel combustion apparatus of this type has a 471□ construction as shown in FIG. That is, a cylindrical bottomed vaporization chamber 1
A heating heater 2 is installed in the circumferential direction of the ventral surface, and a mixing plate 3 having a diaphragm shape is installed in the open surface. Further, a blower pipe 4 is connected to a part of the vaporizing chamber 1, and combustion air is sent into the vaporizing chamber 1 from the blower fan 5, and a fuel nozzle 6 is passed through the blower tube 4 and directed into the vaporizing chamber 1. ing. The fuel is vaporized together with combustion air on the vaporization surface 7 provided on the inner wall of the vaporization chamber 1, and while being mixed is supplied to a part of the combustion section 8 and combusted.

この構成において、定常燃焼時に気化面7は、加熱用ヒ
ータ2や、燃焼火炎により前部となっている燃焼部8か
らの熱伝導等の影響ヲ受けて温度が冒〈なっている。し
かし気化室1にn(4出した燃料が直接衝突する気化面
1の近傍、すなわち衝突面7aは、噴出してきた燃料や
燃焼空気がWj、接衝突することにより熱を奪われ易く
、特に、燃料の気化に際しての気化熱を多句に蜘わf’
していた。このため、この衝突面7aは温度が他の気化
面7よりも低くなり易く、燃料が温度と空気の影響を受
けてタール化し、クールの蓄積による着火、消火時の臭
気、−酸化炭素等有害物質の発生、燃焼時の有毒酸化物
の発生が著しいという問題があった。
In this configuration, during steady combustion, the temperature of the vaporization surface 7 is affected by heat conduction from the heater 2 and the combustion section 8 which is the front part due to the combustion flame. However, the vicinity of the vaporization surface 1 where the fuel ejected into the vaporization chamber 1 directly collides with the vaporization surface 1, that is, the collision surface 7a, is likely to lose heat due to the direct collision of the ejected fuel and combustion air. The heat of vaporization during fuel vaporization is expressed in many words.
Was. Therefore, the temperature of this collision surface 7a tends to be lower than that of other vaporization surfaces 7, and the fuel is affected by the temperature and air and turns into tar, causing ignition due to the accumulation of cool, odor during extinguishing, and other harmful substances such as carbon oxide. There were problems with the generation of substances and the generation of toxic oxides during combustion.

発明の目的 本発明はこの様な従来の問題を解決したもので、気化面
へのタール蓄積全抑制し、良質な燃焼を提供すること全
目的とする。
OBJECTS OF THE INVENTION The present invention solves these conventional problems, and its overall purpose is to completely suppress tar accumulation on the vaporization surface and provide high-quality combustion.

発明の構成 この目的を達成するために本発明は、気化室内に燃料と
燃焼空気を気化室の内周気化面に沿って噴出させ、旋回
させながら気化させるとともに、燃料が気化面に直接衝
突する位置を、燃焼空気が気化面に直接衝突する位置よ
りも旋回方向にすらしたものである。
Structure of the Invention In order to achieve this object, the present invention injects fuel and combustion air into the vaporization chamber along the inner circumferential vaporization surface of the vaporization chamber, vaporizes it while swirling, and causes the fuel to collide directly with the vaporization surface. The position is further in the swirling direction than the position where the combustion air directly impinges on the vaporizing surface.

実施例の説明 以下、本発明の一実施例について第2図に基づいて説明
する。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG.

1は円筒有底状の気化室で、腹面部円周方向に加熱用ヒ
ータ2を装設し、開放面に絞り形状を有する混合板3を
製箔している。さらに気化室1の一部に送風管4を接合
して、これより気化室1因に燃焼空気を送風ファン5よ
り送るとともに、燃料ノズル6を送風管4中を通して気
化室1内にのぞ1せている。燃料は燃焼空気とともに送
風管4より気化室1の内周に沿って噴出され、旋回しな
がら気化室1の内壁に設けられた気化面7て気化され、
混合されながら上部の燃焼部8に供給され、燃焼する。
Reference numeral 1 denotes a cylindrical vaporization chamber with a bottom, a heating heater 2 is installed in the circumferential direction of the ventral surface, and a mixing plate 3 having an aperture shape on the open surface is formed into foil. Furthermore, a blower pipe 4 is connected to a part of the vaporization chamber 1, from which combustion air is sent to the vaporization chamber 1 from a blower fan 5, and a fuel nozzle 6 is passed through the blower tube 4 into the vaporization chamber 1. It's set. The fuel is ejected along the inner circumference of the vaporization chamber 1 from the blast pipe 4 together with combustion air, and is vaporized on the vaporization surface 7 provided on the inner wall of the vaporization chamber 1 while swirling.
The mixture is supplied to the upper combustion section 8 and combusted.

このとき、燃料が気化ml 7に直接衝突する位+1.
:、l、すなわち燃料衝突面9は、燃焼空気が気化面7
に直接衝突する位置、ナな4つら空気衝突面10よりも
わずかに旋回方向にすらしである。
At this time, the fuel directly collides with the vaporized ml 7 +1.
:, l, that is, the fuel collision surface 9 is the combustion air vaporization surface 7.
The position of direct impact is slightly in the direction of rotation than the four air impact surfaces 10.

この構成により、気化室1における加熱用ヒータ2への
通電により気化室1が加熱される。この後送風管4を介
して設けられた送風ファン5を駆動させることにより気
化41内に燃焼空気が送入される。続いて燃料ノズIし
6より燃料は気化¥1内に旋回しながら噴出される。燃
料は気化面7により温度の影響を受けて気化ガスとなり
、」二部に配した混合板3の絞り都を通過して燃焼部8
へ流れ出る。このとき燃料気化ガスは、燃焼空気と混合
され、混合気化ガスとして燃焼部8において燃焼火炎を
形成する。
With this configuration, the vaporization chamber 1 is heated by supplying electricity to the heater 2 in the vaporization chamber 1. Thereafter, combustion air is introduced into the vaporizer 41 by driving a blower fan 5 provided through the blower pipe 4 . Subsequently, the fuel is spouted from the fuel nozzle I and 6 while swirling into the vaporized space. The fuel becomes a vaporized gas through the vaporization surface 7 under the influence of temperature, passes through the throttle of the mixing plate 3 arranged in the second section, and is then transferred to the combustion section 8.
flows out to At this time, the fuel vaporized gas is mixed with combustion air to form a combustion flame in the combustion section 8 as a mixed vaporized gas.

この際燃料の気化は気化面7においてなされるが、燃料
が気化面7に直接衝突する燃料衝突面9が、燃焼空気の
気化面7に直接衝突する空気衝突面10よりもわずかに
旋回方向にすれているため、気化面7の局部的な冷却現
象が緩和され、気化面7へのタール生成・蓄積が著しく
峨少するとともに、燃料衝突面9へ噴出した燃料は、燃
焼空気による旋回流により、すべて旋回方向に分散して
いき、燃料の気化形態が安定し、気化の変動がなくなっ
た。
At this time, the fuel is vaporized on the vaporization surface 7, but the fuel impingement surface 9, where the fuel directly collides with the vaporization surface 7, is slightly tilted in the swirling direction relative to the air impingement surface 10, where the combustion air directly collides with the vaporization surface 7. Because of this, the local cooling phenomenon of the vaporization surface 7 is alleviated, and the generation and accumulation of tar on the vaporization surface 7 is significantly reduced, and the fuel ejected to the fuel collision surface 9 is caused by the swirling flow caused by the combustion air. , all of the fuel was dispersed in the direction of rotation, and the vaporization form of the fuel became stable, with no fluctuations in vaporization.

ここで燃料と燃焼空気の流れを従来例と比較して詳述す
る。従来例においては第3図に示されるように、気化室
1内に噴出した燃料と燃焼空気はほぼ回−気化面7上に
直接衝突する。このため衝突面7aは燃料と燃焼空気に
よる著しい冷却作用全骨け、タールが生成、蓄積し易く
なっていた。
Here, the flow of fuel and combustion air will be explained in detail in comparison with the conventional example. In the conventional example, as shown in FIG. 3, the fuel and combustion air injected into the vaporization chamber 1 almost directly collide with the vaporization surface 7. For this reason, the collision surface 7a is susceptible to the significant cooling effect of the fuel and combustion air, making it easy for tar to form and accumulate.

また、衝突面7aに衝突後、燃料と燃焼空気は、大部分
が旋回流の方向へ飛散していくが、他の方向にも燃料や
燃焼空気は飛散するため、旋回方向の反対側には旋回流
と反対の流れが生じ、この反旋回流中に飛散した燃料は
十分分散されないま捷、再結泉して、大きな粒子となっ
て気化ffi]7.41にたまり、気化の乱れを生じる
要因となっていた。しかし第4図に示されるように、本
実施例によると、気化室1因に噴出した燃料と燃焼空気
は、それぞれ燃料衝突面9、空気衝突面10に直接衝突
するため気化面7における局部的な冷却が緩和され、気
化面7全体の温間分布の差が械少し、タール生成、蓄積
が著しく蟻少する。1だ、燃料衝突用19へ噴出した燃
料は、燃焼を気による旋回流によりすべて旋回方向に分
散し、気化するため燃料の気化形態が安定し、気化の変
UJがなくなる。さらに燃焼空気の噴出方向を、燃料の
噴出方向よりも下方に向けることによって、気化室1底
而部における燃料の気化作用が促進でき、より安定な気
化を得ることができる。
Furthermore, after colliding with the collision surface 7a, most of the fuel and combustion air are scattered in the direction of the swirling flow, but since the fuel and combustion air are also scattered in other directions, there are A flow opposite to the swirling flow occurs, and the fuel scattered in this counter-swirling flow is not sufficiently dispersed and recondenses, becoming large particles and accumulating in the vaporization ffi]7.41, causing turbulence in vaporization. This was a contributing factor. However, as shown in FIG. 4, according to this embodiment, the fuel and combustion air ejected into the vaporization chamber 1 collide directly with the fuel impingement surface 9 and the air impingement surface 10, respectively. Cooling is relaxed, the difference in warm distribution across the vaporization surface 7 is reduced, and tar generation and accumulation are significantly reduced. 1, the fuel injected into the fuel collision 19 is completely dispersed in the swirling direction due to the swirling flow caused by air and is vaporized, so the vaporization form of the fuel is stabilized and the variation UJ of vaporization is eliminated. Furthermore, by directing the jetting direction of the combustion air downward than the jetting direction of the fuel, the vaporization action of the fuel in the bottom portion of the vaporization chamber 1 can be promoted, and more stable vaporization can be obtained.

発明の効果 本発明の液体燃料燃焼装置によれは、燃料と燃焼空気を
気化室の内周気化面に沿って噴出せしめ、旋回させなが
ら気化させるとともに、燃料が気化1−(riに直接衝
突する位置を、燃焼空気が気化面に直接衝突する位置よ
りも旋回方向にすらすことにより、下記の効果を有する
Effects of the Invention According to the liquid fuel combustion device of the present invention, the fuel and combustion air are ejected along the inner circumferential vaporization surface of the vaporization chamber, vaporized while swirling, and the fuel directly collides with the vaporization 1-(ri). By locating the combustion air in the swirling direction rather than the position where the combustion air directly impinges on the vaporizing surface, the following effects can be obtained.

(1) 気化面の燃料や燃焼空気による局部的な冷却現
象か緩和され、燃料が低い温度域において、空気の影響
を受けてクール化することなく、気化面全体が燃料の気
化に有効に作用することにより、気化1mでのタール生
成・蓄積が、はとんどなくなり雇「火、消火、燃焼時の
臭気、−酸化炭素等の有毒物質の発生が著しく蛾少する
(1) The local cooling phenomenon caused by the fuel and combustion air on the vaporizing surface is alleviated, and the entire vaporizing surface effectively works to vaporize the fuel in a low temperature range without being cooled by the influence of air. By doing so, the formation and accumulation of tar at 1 meter of vaporization is completely eliminated, and the generation of toxic substances such as fire, extinguishing, and combustion odors and carbon oxides is significantly reduced.

(2)燃料の飛散方向が一定化することにより、燃料が
再結集して大きな粒子となって気化面」二に滞留するこ
とがなくなるため、燃料の気化形態が安定し、気化の変
動がなくなり、燃焼火炎の脈動や空燃比の乱れによる一
酸化炭素の発生が防止でき、燃焼特性の向上がはかれる
(2) By keeping the scattering direction of the fuel constant, the fuel will no longer aggregate into large particles and stay on the vaporization surface, which will stabilize the vaporization form of the fuel and eliminate fluctuations in vaporization. The generation of carbon monoxide due to combustion flame pulsations and air-fuel ratio disturbances can be prevented, and combustion characteristics can be improved.

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

第1図は従来の液体燃料燃焼装置を示す断面図、第2図
は本発り」の一実施例の液体燃料燃焼装置を示す断面図
、第3図は従来の液体燃料燃焼装置1′1”の気化室の
断面図、第4図は本発明の一実施例の装置の気化室の断
面図である。 1・ ・気化釡、4・・・・送風管、6・・ 燃料ノズ
ル、7・・ 気化面、9・・・・燃料衝突面、10・・
・・空気衝突面。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第 2 図
Fig. 1 is a sectional view showing a conventional liquid fuel combustion device, Fig. 2 is a sectional view showing a liquid fuel combustion device according to an embodiment of the present invention, and Fig. 3 is a conventional liquid fuel combustion device 1'1. Figure 4 is a cross-sectional view of the vaporization chamber of an apparatus according to an embodiment of the present invention. ... Vaporization surface, 9...Fuel collision surface, 10...
...Air collision surface. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2

Claims (2)

【特許請求の範囲】[Claims] (1)加熱手段を備えた円筒有底状の気化室内に、燃料
と燃焼空気を気化室の内周気化面に沿って噴出させ、旋
回させながら気化させるとともに、燃料が気化面に直接
衝突する位置を、燃焼空気が気化面に直接衝突する位置
よりも旋回方向にずらした液体燃料燃焼装置。
(1) Fuel and combustion air are ejected into a cylindrical bottomed vaporization chamber equipped with a heating means along the inner circumferential vaporization surface of the vaporization chamber, vaporized while swirling, and the fuel collides directly with the vaporization surface. A liquid fuel combustion device in which the position of the combustion air is shifted in the direction of rotation from the position where the combustion air directly collides with the vaporizing surface.
(2)燃焼空気の噴出方向を、燃料の噴出方向よりも下
方に向けた特許請求の範囲第1項記載の液体燃料燃焼装
置。
(2) The liquid fuel combustion device according to claim 1, wherein the direction in which the combustion air is ejected is directed downward than the direction in which the fuel is ejected.
JP5470684A 1984-03-21 1984-03-21 Liquid fuel burner Pending JPS60200012A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5470684A JPS60200012A (en) 1984-03-21 1984-03-21 Liquid fuel burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5470684A JPS60200012A (en) 1984-03-21 1984-03-21 Liquid fuel burner

Publications (1)

Publication Number Publication Date
JPS60200012A true JPS60200012A (en) 1985-10-09

Family

ID=12978239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5470684A Pending JPS60200012A (en) 1984-03-21 1984-03-21 Liquid fuel burner

Country Status (1)

Country Link
JP (1) JPS60200012A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0346284A2 (en) * 1988-06-09 1989-12-13 Füllemann Patent Ag Burner for the combustion of liquid fuel in the gaseous phase
US5154597A (en) * 1987-03-13 1992-10-13 Vth Ag Verfahrenstechnik Fur Heizung Burner for combustion of gasified liquid fuels

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5154597A (en) * 1987-03-13 1992-10-13 Vth Ag Verfahrenstechnik Fur Heizung Burner for combustion of gasified liquid fuels
EP0346284A2 (en) * 1988-06-09 1989-12-13 Füllemann Patent Ag Burner for the combustion of liquid fuel in the gaseous phase

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