JPS61180821A - Liquid fuel burning device - Google Patents
Liquid fuel burning deviceInfo
- Publication number
- JPS61180821A JPS61180821A JP3792686A JP3792686A JPS61180821A JP S61180821 A JPS61180821 A JP S61180821A JP 3792686 A JP3792686 A JP 3792686A JP 3792686 A JP3792686 A JP 3792686A JP S61180821 A JPS61180821 A JP S61180821A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- fuel
- odor
- generation
- offensive odor
- 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
Landscapes
- Wick-Type Burners And Burners With Porous Materials (AREA)
- Spray-Type Burners (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は液体燃料燃焼装置に関するもので、その目的は
消火時に臭気を排出しない液体燃料燃焼装置を提供する
ことにある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a liquid fuel combustion device, and an object thereof is to provide a liquid fuel combustion device that does not emit odor when extinguishing a fire.
石油等の液体燃料を使用する燃焼装置は広範な用途で実
用されているが、特に消火時には強い悪臭を発生する欠
点があった。Combustion devices that use liquid fuels such as petroleum are used in a wide range of applications, but they have the drawback of emitting a strong odor, especially when extinguishing fires.
本発明はこの消火時の臭気発生を防止するものであり、
以下本発明の一実施例を添付図面にもとづいて説明する
。The present invention prevents the occurrence of this odor during extinguishing,
An embodiment of the present invention will be described below based on the accompanying drawings.
第1図は本発明の一実施例についてその構成を示したも
のである。先ず燃料系について説明する。FIG. 1 shows the configuration of an embodiment of the present invention. First, the fuel system will be explained.
1は燃料タンクで、液体燃料はポンプ2により燃料供給
部3へ送られる。4はオーバーフロー形式の定油面装置
で、燃料消費に見合う量の燃料を燃料供給部3に供給す
るが、過剰の燃料はリターン流路6を通じて燃料タンク
1へもどされる。6は多孔体で、下端部が燃料供給部3
の燃料に浸漬されており、上端部の燃料気化部7に燃料
を吸上げる。8は燃料気化部7に近接して備えた発熱体
で、通電により発熱して気化に必要な熱を燃料気化部7
に与えるものである。1 is a fuel tank, and liquid fuel is sent to a fuel supply section 3 by a pump 2. Reference numeral 4 denotes an overflow type constant oil level device that supplies fuel in an amount commensurate with fuel consumption to the fuel supply section 3, but excess fuel is returned to the fuel tank 1 through a return passage 6. 6 is a porous body, the lower end of which is the fuel supply part 3
The fuel is immersed in the fuel, and the fuel is sucked up into the fuel vaporization section 7 at the upper end. Reference numeral 8 denotes a heating element provided close to the fuel vaporization section 7, which generates heat when energized and transfers the heat necessary for vaporization to the fuel vaporization section 7.
It is given to
次に空気系について説明する。9は給気口、10は送風
機、11.12は送風管、13は切換管、14.15は
弁である。なお、送風管11の燃料気化部7に対向する
部分には多数の小孔が設けられている。また、第1図に
示した矢印は燃焼時の空気の流れ方向を示したものであ
る。Next, the air system will be explained. 9 is an air supply port, 10 is a blower, 11.12 is a blower pipe, 13 is a switching pipe, and 14.15 is a valve. Note that a large number of small holes are provided in a portion of the blast pipe 11 facing the fuel vaporization section 7. Further, the arrows shown in FIG. 1 indicate the direction of air flow during combustion.
次に燃焼系について説明する。16は下部混合室、17
は上部混合室で、燃料気化部7から気化した燃料と送風
管11.12から供給された空気が上記両混合室16.
17で充分混合され、次に炎口部18を通過して燃焼空
間19で燃焼するように構成されている。なお、2oは
複数の小孔を有する隔板、21は隔室で、送風管12か
ら隔室21に入った空気は、隔板2oの小孔から下部混
合室16に導入されるように構成されている。また、2
2は排出口である。Next, the combustion system will be explained. 16 is the lower mixing chamber, 17
is an upper mixing chamber in which the fuel vaporized from the fuel vaporization section 7 and the air supplied from the blast pipe 11.12 are mixed into both the mixing chambers 16.
The fuel is sufficiently mixed at step 17 , and then passes through a flame port 18 and burns in a combustion space 19 . Note that 2o is a partition plate having a plurality of small holes, and 21 is a partition chamber, and the air that has entered the partition chamber 21 from the blower pipe 12 is introduced into the lower mixing chamber 16 through the small holes in the partition plate 2o. has been done. Also, 2
2 is a discharge port.
第2図は第1図の実施例における消火時の空気の流れ方
向と弁14.15の位置を示したもので、第1図に示し
た燃焼時の空気の流れ方向および弁14.16と対比し
て理解しやすいように示した。Figure 2 shows the direction of air flow during fire extinguishing and the position of valve 14.15 in the embodiment shown in Figure 1. I have provided a comparison to make it easier to understand.
なお、この実施例の点火方法はポン129発熱体8.送
風機10.炎口部1Cに近接して設けられた高圧間欠放
電点火器(図示せず)への通電と、弁1−J−,1gの
位置セットを第1図の状態にすることにより行なわれる
。更に消火方法は上記の通電の停止と弁14.ISは第
2図の状態にすることにより行なわれる。この時、送風
機1oは駆動電源を切断されるが慣性力により暫時駆動
を継続し、これにより第2図に示した矢印方向に気体の
流動が行なわれるのである。Incidentally, the ignition method in this embodiment is a Pon 129 heating element 8. Blower10. This is done by energizing a high-pressure intermittent discharge igniter (not shown) provided close to the flame port 1C and setting the valves 1-J- and 1g in the position shown in FIG. Furthermore, the fire extinguishing method is to stop the energization mentioned above and valve 14. IS is performed by setting the state as shown in FIG. At this time, the drive power to the blower 1o is cut off, but the blower 1o continues to be driven for a while due to its inertial force, thereby causing the gas to flow in the direction of the arrow shown in FIG.
次に本実施例の効果を説明する。Next, the effects of this embodiment will be explained.
先ず、従来例における消火時に発生する臭気の発生メカ
ニズムを明らかにする。第3図は従来例の燃焼空間へ供
給される混合気の空気過剰率を縦軸に、消火前後の時間
経過を横軸に示したものである。同図において継続燃焼
段階Aは空気過剰率が適正値で安定しており、実用上の
完全燃焼状態を示して臭気の発生も実用上皆無と言える
が、消火操作(a点)を行なって消火過渡段階Bに入る
と、燃焼量が減少すると同時に空気過剰率が増大しく逆
に変動する場合もある)消火(b点)に至る。しかし、
消火以前に燃焼火炎のリフト現象が生じて臭気発生段階
Cに入り、消火以後もなお燃料成分の燃焼空間への放出
が継続し、燃焼時加熱された高温部からの熱で加熱され
ることにより、単なる気化燃料とは異なる臭気成分(例
えばアルデヒド等)に変化し、極めて強い臭気を発生す
る。First, we will clarify the mechanism behind the odor generated during conventional fire extinguishing. FIG. 3 shows the excess air ratio of the mixture supplied to the combustion space in the conventional example on the vertical axis and the horizontal axis as the elapsed time before and after extinguishing the fire. In the same figure, in the continuous combustion stage A, the excess air ratio is stable at an appropriate value, indicating a practically complete combustion state, and practically no odor is generated. When entering transition stage B, the combustion amount decreases and at the same time the excess air ratio increases and may even fluctuate in the opposite direction) leading to extinguishment (point b). but,
Before extinguishing, the combustion flame lift phenomenon occurs and enters odor generation stage C, and even after extinguishing, fuel components continue to be released into the combustion space, and are heated by heat from the high temperature part heated during combustion. , it changes into an odor component (for example, aldehyde, etc.) different from that of simple vaporized fuel, and generates an extremely strong odor.
なお、燃料成分から臭気成分に変化する加熱条件は時間
の関数的要素もあるので単純に表現し難いが、燃料成分
の沸点以上の温度に加熱しないことにより、臭気成分に
変化することが防止できる。Note that the heating conditions under which a fuel component changes into an odor component are difficult to express simply because it is a function of time, but by not heating the fuel component to a temperature above the boiling point, it is possible to prevent the fuel component from changing into an odor component. .
次に、本発明実施例の場合を説明すると、第3図と同じ
尺度で示した第4図に示すごとく消火操作(a点)を行
なうと燃焼量は減少し、空気過剰率も変動するが、臭気
発生段階Bに入る以前に第2図のごとく送風機1oによ
って臭気発生原因となる燃料成分は別離路(送風管11
.12)に吸引されるので、空気過剰率が急激に極大状
態に増大しく燃料成分のない空気のみの状態となり)、
同時に消火する。従って臭気の発生は皆無の状態に改善
されることになる。Next, to explain the case of the embodiment of the present invention, as shown in FIG. 4, which is shown on the same scale as FIG. Before entering the odor generation stage B, as shown in Fig. 2, the fuel components that cause odor generation are separated by the blower 1o (the
.. 12), the excess air ratio rapidly increases to the maximum state and becomes a state where there is only air with no fuel components),
Extinguish the fire at the same time. Therefore, the occurrence of odor will be improved to zero.
別離路(11,12)に吸引された燃料成分は加熱され
ることなく外部に放出されるので燃料の単なる気化状態
または微粒化状態で極めて弱い臭気に止どまるのでかな
りの臭気低減効果が得られる。即ち別離路(11,12
)から放出する場合は燃焼中に高温になった炎口部18
あるいは燃焼空間19に近接した部分からの高温の影響
を受は加熱されることがないので、燃料成分から臭気成
分に変化する反応が発生しない状態で放出することがで
きる。この際、吸引から排出までの流路中で一部の燃料
成分が凝縮し固体面に付着する現象が生じ易いが、この
現象の発生は何ら本発明の本質をさまたげるものではな
い。The fuel components sucked into the separate passages (11, 12) are discharged to the outside without being heated, so the mere vaporization or atomization of the fuel produces only an extremely weak odor, resulting in a considerable odor reduction effect. It will be done. That is, separation route (11, 12
), the flame opening 18 that became high temperature during combustion.
Alternatively, since the fuel is not heated under the influence of high temperatures from the portions close to the combustion space 19, it can be discharged without any reaction that changes the fuel components into odor components. At this time, some fuel components tend to condense in the flow path from suction to discharge and adhere to the solid surface, but the occurrence of this phenomenon does not impede the essence of the present invention in any way.
なお、送風機10とは別に吸引器を設けることも考えら
れるが、実施例のように送風機10により燃焼中は送風
装置として動作し、消火に際しては吸引装置として動作
するような構成を形成する方が、コスト、スペース、動
作タイミング調整等の面でのメリットが大きい。Although it is possible to provide a suction device separately from the blower 10, it is better to form a configuration in which the blower 10 operates as a blower device during combustion and as a suction device when extinguishing a fire, as in the embodiment. , it has great advantages in terms of cost, space, operation timing adjustment, etc.
更に、消火時において上記送風機10を吸引装置として
動作させたときに燃焼空間19から混合室16.17へ
の逆火を生じて爆発の恐れを解消するために吸引量を適
正に設計することが効果的であり、本願実施例の場合は
排出口22に絞り部分を設けることにより吸引量の適正
化を実施している。Furthermore, when the blower 10 is operated as a suction device during fire extinguishing, the suction amount must be appropriately designed to eliminate the risk of explosion due to backfire from the combustion space 19 to the mixing chamber 16,17. This is effective, and in the case of the embodiment of the present application, the amount of suction is optimized by providing a constriction portion in the discharge port 22.
以上のように本発明によれば消火時の臭気を大幅に低減
し得る効果を有するものである。As described above, the present invention has the effect of significantly reducing odor during fire extinguishing.
第1図は本発明の一実施例にかかる液体燃料燃焼装置の
要部断面図、第2図は同液体燃料燃焼装置の消火時の動
作を説明する断面図、第3図は従来例の消火臭気の発生
メカニズムを説明する図、第4図は本発明の消火臭気効
果を説明する図である。
10・・・・・・送風機(吸引装置)、16・・・・・
・下部混合室、17・・・・・・上部混合室、19・・
・・・・燃焼空間、22・・・・・・排出口。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名区
ゝ
第3図
峙間□FIG. 1 is a cross-sectional view of a main part of a liquid fuel combustion device according to an embodiment of the present invention, FIG. 2 is a cross-sectional view illustrating the operation of the same liquid fuel combustion device during fire extinguishing, and FIG. 3 is a conventional example of fire extinguishing. FIG. 4 is a diagram illustrating the odor generation mechanism, and FIG. 4 is a diagram illustrating the fire extinguishing odor effect of the present invention. 10...Blower (suction device), 16...
・Lower mixing chamber, 17... Upper mixing chamber, 19...
...Combustion space, 22...Exhaust port. Name of agent: Patent attorney Toshio Nakao and 1 other person
ゝFigure 3 Sekima □
Claims (1)
移動する空間に、燃焼継続中は不動作状態の吸引装置を
連結し、消火時に上記吸引装置を動作させて上記状態の
液体燃料と空気の混合気体を吸引し、この気体を加熱す
ることなく外部へ排出することを特徴とする液体燃料燃
焼装置。A suction device, which is inactive while combustion continues, is connected to the space where the liquid fuel moves toward the combustion part in a gaseous or particulate state, and when the fire is extinguished, the suction device is activated to remove the liquid fuel in the above state and the air. A liquid fuel combustion device characterized by sucking a mixed gas and discharging this gas to the outside without heating it.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3792686A JPS61180821A (en) | 1986-02-21 | 1986-02-21 | Liquid fuel burning device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3792686A JPS61180821A (en) | 1986-02-21 | 1986-02-21 | Liquid fuel burning device |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4952279A Division JPS55140011A (en) | 1979-04-20 | 1979-04-20 | Liquid fuel combustion device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61180821A true JPS61180821A (en) | 1986-08-13 |
JPS6242201B2 JPS6242201B2 (en) | 1987-09-07 |
Family
ID=12511154
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3792686A Granted JPS61180821A (en) | 1986-02-21 | 1986-02-21 | Liquid fuel burning device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61180821A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5027901A (en) * | 1973-07-13 | 1975-03-22 | ||
JPS5237233A (en) * | 1975-09-19 | 1977-03-23 | Matsushita Electric Ind Co Ltd | Fire-extinguishing apparatus in burner |
JPS5372237U (en) * | 1976-11-19 | 1978-06-16 |
-
1986
- 1986-02-21 JP JP3792686A patent/JPS61180821A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5027901A (en) * | 1973-07-13 | 1975-03-22 | ||
JPS5237233A (en) * | 1975-09-19 | 1977-03-23 | Matsushita Electric Ind Co Ltd | Fire-extinguishing apparatus in burner |
JPS5372237U (en) * | 1976-11-19 | 1978-06-16 |
Also Published As
Publication number | Publication date |
---|---|
JPS6242201B2 (en) | 1987-09-07 |
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