JPH0460307A - Liquid fuel burner - Google Patents

Liquid fuel burner

Info

Publication number
JPH0460307A
JPH0460307A JP17092190A JP17092190A JPH0460307A JP H0460307 A JPH0460307 A JP H0460307A JP 17092190 A JP17092190 A JP 17092190A JP 17092190 A JP17092190 A JP 17092190A JP H0460307 A JPH0460307 A JP H0460307A
Authority
JP
Japan
Prior art keywords
air
exhaust gas
combustion
evaporation chamber
liquid fuel
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
JP17092190A
Other languages
Japanese (ja)
Inventor
Kosaku Shirode
城出 浩作
Seiichiro Kumagai
熊谷 清一郎
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 JP17092190A priority Critical patent/JPH0460307A/en
Publication of JPH0460307A publication Critical patent/JPH0460307A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To make it possible to heat the air by the high temperature exhaust gas that is formed at the combustion section after combustion is started and reduce electric power consumption due to the use of an electric heater by providing an exhaust gas circulation means which mixes part of the high temperature exhaust gas produced in the combustion section with the air that is taken in and circulates the mixture. CONSTITUTION:When the operation is started and the combustion is started, the high temperature exhaust gas that is formed in a combustion section 50 is mixed with air in an exhaust gas circulation means (consisting of an exhaust gas channel 71 and a control valve 72) and the mixture gas is circulated, and the air that is sent to an evaporation chamber 20 is suitably heated by the high temperature exhaust gas. With this arrangement in the steady combustion except the initial stage of ignition right after starting the operation it can be continued without using an electric heating means 30 or with a small consumption of electric power. And, since the heating of the air by mixing the high temperature exhaust gas is direct, it is possible to heat the air by following without delay a rapid increase of fuel.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、加熱された空気中に石油等の液体燃料を微粒
化して供給し、比較的低い温度で液体燃料を蒸発させ、
燃焼を行う方式の液体燃料燃焼装置に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention provides a method for supplying atomized liquid fuel such as petroleum into heated air, evaporating the liquid fuel at a relatively low temperature,
The present invention relates to a liquid fuel combustion device that performs combustion.

〈従来の技術〉 この種装置の従来例を第5図、第6図を用いて説明する
。第5図は従来装置の断面構成図、第6図は第5図のC
−C断面図である。
<Prior Art> A conventional example of this type of device will be described with reference to FIGS. 5 and 6. Figure 5 is a cross-sectional diagram of the conventional device, and Figure 6 is C of Figure 5.
-C sectional view.

空気がファン11で取り入れられ、供給路12を通って
蒸発室20に送り込まれる。30は電気ヒータで、空気
を途中で加熱するためのものである。一方、石油等の液
体燃料が噴射ノズル40を介して微粒化状態で蒸発室2
0内に噴出せられる。蒸発室20内では、導入された微
粒化燃料が同じく導入された加熱空気によって直接的に
接触蒸発せられる。そして気化された燃料は燃焼部50
に送られ、燃焼に供される。前記電気ヒータ30で加熱
される空気の温度は温度センサ60により制御される。
Air is taken in by a fan 11 and sent into the evaporation chamber 20 through a supply path 12. 30 is an electric heater for heating the air midway. On the other hand, liquid fuel such as petroleum is atomized into the evaporation chamber 2 through the injection nozzle 40.
It is ejected within 0. In the evaporation chamber 20, the introduced atomized fuel is directly catalytically evaporated by the heated air also introduced. Then, the vaporized fuel is transferred to the combustion section 50.
and is sent to be burned. The temperature of the air heated by the electric heater 30 is controlled by a temperature sensor 60.

〈発明が解決しようとする課題〉 ところが上記従来の装置では、空気の加熱を電気ヒータ
で行っているため、運転中は絶えず電力を消費し、経済
性が悪いという欠点があった。また燃料の供給量が多く
なって(ると、電気ヒータの消費電力が増加し、一般家
庭用では電気配線の容量が不足する欠点があった。
<Problems to be Solved by the Invention> However, in the conventional apparatus described above, since air is heated by an electric heater, electric power is constantly consumed during operation, which is disadvantageous in that it is not economical. In addition, as the amount of fuel supplied increased, the power consumption of the electric heater increased, and for general household use, there was a drawback that the capacity of the electric wiring was insufficient.

そこで本発明は上記従来装置の欠点を解消し、燃料供給
量が多くなっても、消費電力の心配をしなくて済み、且
つ定常時に電力の消費が少ない液体燃料燃焼装置の提供
を目的とする。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a liquid fuel combustion device that eliminates the drawbacks of the conventional devices described above, eliminates the need to worry about power consumption even when the amount of fuel supplied is large, and consumes less power in steady state. .

〈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
、室内に導入された微粒化液体燃料を同じく室内に導入
された加熱空気で直接的に接触蒸発させる蒸発室と、空
気を外部から取り入れて前記蒸発室へ送り込む空気送り
込み手段と、外部から取り入れた空気を途中で加熱する
ために設けられる電気的加熱手段と、液体燃料を微粒化
状態で前記蒸発室内に噴射する燃料導入手段と、前記蒸
発室で気化された燃料を燃焼させる燃焼部とを有する液
体燃料燃焼装置であって、前記燃焼部で生じた高温排ガ
スの一部を前記取り入れられる空気に混合して循環させ
る排ガス循環手段を設けたことを第1の特徴としている
<Means for Solving the Problems> In order to achieve the above object, the liquid fuel combustion device of the present invention directly catalytically evaporates the atomized liquid fuel introduced into the room with heated air also introduced into the room. an evaporation chamber; an air feeding means for taking in air from the outside and sending it into the evaporation chamber; an electric heating means provided to heat the air taken in from the outside midway; A liquid fuel combustion device comprising a fuel introduction means for injecting fuel into the evaporation chamber, and a combustion section for burning the fuel vaporized in the evaporation chamber, wherein a part of high-temperature exhaust gas generated in the combustion section is mixed with the air taken in. The first feature is that an exhaust gas circulation means is provided to circulate the exhaust gas.

また本発明の液体燃料燃焼装置は、上記第1の特徴にお
いて、排ガス循環手段を設ける代わりに、燃焼部で生じ
た高温排熱を用いて送り込まれる空気を加熱する排熱循
環手段を設けたことを第2の特徴としている。
Furthermore, in the liquid fuel combustion apparatus of the present invention, in the first feature, instead of providing the exhaust gas circulation means, an exhaust heat circulation means is provided for heating the air sent in using high temperature waste heat generated in the combustion section. is the second feature.

〈作用〉 上記第1の特徴によれば、運転が開始され、燃焼が開始
されると、燃焼部で生じた高温排ガスを排ガス循環手段
で空気と混合して循環させることができるので、蒸発室
へ送られる空気が高温排ガスによって適当に加熱される
。よって、運転開始後の着火初期段階を除く定常燃焼中
は、電気的加熱手段を用いることなく、或いは少ない消
費電力で運転を続けることができる。また高温排ガス混
合による空気の加熱は電気ヒータ等による場合に比較し
て直接的であるので、燃料の急激な増加に対しても素早
く追従して空気を加熱することができる。
<Operation> According to the first feature, when the operation is started and combustion is started, the high-temperature exhaust gas generated in the combustion section can be mixed with air and circulated by the exhaust gas circulation means, so that the evaporation chamber The air sent to the system is appropriately heated by the high-temperature exhaust gas. Therefore, during steady combustion excluding the initial stage of ignition after the start of operation, operation can be continued without using electrical heating means or with less power consumption. Furthermore, since heating of the air by mixing high-temperature exhaust gas is more direct than when using an electric heater or the like, it is possible to quickly follow a sudden increase in fuel and heat the air.

上記第2の特徴によれば、上記第1の特徴における排ガ
スの代わりに排熱が循環されるので、上記第1の特徴に
おける作用と同様な作用がなされる。しかもその場合、
排ガスは循環されないので、蒸発室へ送られる空気がク
リーンである。
According to the second feature, exhaust heat is circulated instead of the exhaust gas in the first feature, so the same effect as in the first feature is achieved. Moreover, in that case,
Since the exhaust gas is not recycled, the air sent to the evaporation chamber is clean.

〈実施例〉 第1図は本発明の第1の実施例を示す断面構成図で、第
2図は第1図のA−A断面図である。第5図、第6図に
示す従来例と同じ部材、要素には同一の符号を付す。
<Embodiment> FIG. 1 is a cross-sectional configuration diagram showing a first embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along the line AA in FIG. 1. The same members and elements as in the conventional example shown in FIGS. 5 and 6 are given the same reference numerals.

蒸発室20は円筒状の外筒21と円板状の両端壁22か
らなり、外筒21の中心軸上に蒸発室20内に液体を噴
射する噴射ノズル40が設けられている。この噴射ノズ
ル40は燃料導入手段を構成する。
The evaporation chamber 20 consists of a cylindrical outer tube 21 and disk-shaped opposite end walls 22, and an injection nozzle 40 for injecting liquid into the evaporation chamber 20 is provided on the central axis of the outer tube 21. This injection nozzle 40 constitutes fuel introduction means.

前記ファン11には吸い込み室13が設けられている。The fan 11 is provided with a suction chamber 13.

このファン11と吸い込み室13と供給路12で蒸発室
20への空気送り込み手段を構成する。前記吸い込み室
13には外部空気の入口13aと、燃焼部5゜からの排
ガスの入口13bが設けられている。13cはジャマ板
である。
The fan 11, the suction chamber 13, and the supply path 12 constitute means for feeding air into the evaporation chamber 20. The suction chamber 13 is provided with an inlet 13a for external air and an inlet 13b for exhaust gas from the combustion section 5. 13c is a jammer plate.

燃焼部50からは排ガス通路71が前記吸い込み室13
まで延設されている。これによって燃焼部50で発生し
た高温排ガスの一部が排ガス通路71を通って吸い込み
室13に循環される。排ガス通路71の途中には循環す
る排ガス量を制御するための制御弁72が設けられてい
る。この排ガス通路71と制御弁72とは排ガス循環手
段を構成する。
From the combustion section 50, an exhaust gas passage 71 connects to the suction chamber 13.
It has been extended to. As a result, a portion of the high-temperature exhaust gas generated in the combustion section 50 is circulated to the suction chamber 13 through the exhaust gas passage 71. A control valve 72 is provided in the middle of the exhaust gas passage 71 to control the amount of circulating exhaust gas. The exhaust gas passage 71 and the control valve 72 constitute exhaust gas circulation means.

運転が開始されると、ファン11が回転し、空気が吸い
込まれる。そして電気的加熱手段である電気ヒータ6で
加熱された空気は、供給路12を通って蒸発室20に導
入される。蒸発室20内が加熱された空気で充満された
ところで、液体燃料が噴射ノズル40を介して蒸発室2
0内に微粒化状態で導入開始される。そして加熱された
空気と混合され蒸発して気化した液体燃料は燃焼室50
に送られて燃焼する。火炎が安定した後、前記制御弁7
2が開かれ、燃焼排ガスの一部が排ガス通路71を通っ
て前記ファン11の吸い込み室13に送り込まれる。そ
して以後、高温の排ガスと新鮮な常温の空気とが混合さ
れ、適当な温度となって蒸発室20へ導入される。前記
制御弁72が開かれた後は前記電気ヒータ30は通電を
停止又は弱められる。と同時に空気の加熱は、主に、前
記蒸発室20の直前の供給路12に設けた温度センサ6
0によって制御されながら作動する前記制御弁72によ
り、排ガスと常温の空気との混合比率を変化させながら
適温に調節して行う。
When the operation is started, the fan 11 rotates and air is sucked in. The air heated by the electric heater 6, which is an electric heating means, is introduced into the evaporation chamber 20 through the supply path 12. When the inside of the evaporation chamber 20 is filled with heated air, the liquid fuel enters the evaporation chamber 2 through the injection nozzle 40.
Introduction is started in an atomized state within 0%. The liquid fuel mixed with the heated air and evaporated into a combustion chamber 50.
is sent to and burned. After the flame has stabilized, the control valve 7
2 is opened, and part of the combustion exhaust gas is sent into the suction chamber 13 of the fan 11 through the exhaust gas passage 71. Thereafter, the high-temperature exhaust gas and fresh room-temperature air are mixed, brought to an appropriate temperature, and introduced into the evaporation chamber 20. After the control valve 72 is opened, the electric heater 30 is de-energized or weakened. At the same time, the air is heated mainly by a temperature sensor 6 installed in the supply path 12 immediately before the evaporation chamber 20.
The control valve 72, which operates under the control of 0, adjusts the temperature to an appropriate temperature while changing the mixing ratio of the exhaust gas and room temperature air.

なお前記制御弁72の開閉は燃焼部50に設けた炎検知
器に基づいて行うことができる。
Note that the control valve 72 can be opened and closed based on a flame detector provided in the combustion section 50.

第3図は本発明の第2の実施例を示す断面構成図、第4
図は第3図のB−B断面図である。
FIG. 3 is a cross-sectional configuration diagram showing a second embodiment of the present invention, and FIG.
The figure is a sectional view taken along the line BB in FIG. 3.

本実施例では、燃焼部50に熱交換器83を設け、該熱
交換器83で熱交換されて加熱された空気を通路81を
通してファン11の吸い込み室13に導くようにしてい
る。82は通路81を通る熱交換空気の量を制御する制
御弁である。また13bは吸い込み室13に設けた前記
燃焼部50からの熱交換空気の入口である。前記熱交換
器83と通路81と制御弁82は、実質上前記燃焼部5
0で発生した排熱を循環させることから排熱循環手段を
構成する。その他、従来例や第1実施例で既に説明した
部材、要素と同一の機能、作用を示す部材、要素には同
一の符号を付して、第3図、第4図に示している。
In this embodiment, a heat exchanger 83 is provided in the combustion section 50, and the air that has been heat exchanged and heated by the heat exchanger 83 is guided to the suction chamber 13 of the fan 11 through a passage 81. 82 is a control valve that controls the amount of heat exchange air passing through the passage 81. Further, 13b is an inlet for heat exchange air from the combustion section 50 provided in the suction chamber 13. The heat exchanger 83, the passage 81 and the control valve 82 are substantially connected to the combustion section 5.
The exhaust heat circulation means is constituted by circulating the exhaust heat generated at zero. Other members and elements having the same functions and actions as those already explained in the conventional example and the first embodiment are denoted by the same reference numerals and shown in FIGS. 3 and 4.

運転が開始された後、燃焼部50の火炎が安定するまで
は上記第1実施例の場合と同様である。火炎が安定する
と、制御弁82が開かれ、熱交換器83で加熱された空
気(400℃〜1000℃程度)が通路81を通って吸
い込み室13に送り込まれる。そして常温の空気と混合
されて適度な温度となって蒸発室20へ導入される。制
御弁82が開かれた後は、電気ヒータ30は通電を停止
又は弱められる。そして蒸発室20へ導入される空気の
温度調節は、温度センサ60と制御弁82により通路8
1を通って供給される高温空気の量を調節することによ
り行う。前記制御弁82の開閉は燃焼部50に設けた図
示しない炎検知器に基づいて行う。
After the operation is started, the process until the flame in the combustion section 50 becomes stable is the same as in the first embodiment. When the flame becomes stable, the control valve 82 is opened, and air heated by the heat exchanger 83 (approximately 400° C. to 1000° C.) is sent into the suction chamber 13 through the passage 81. The air is then mixed with air at room temperature, brought to an appropriate temperature, and introduced into the evaporation chamber 20. After the control valve 82 is opened, the electric heater 30 is de-energized or weakened. The temperature of the air introduced into the evaporation chamber 20 is controlled by a temperature sensor 60 and a control valve 82.
This is done by adjusting the amount of hot air fed through 1. The control valve 82 is opened and closed based on a flame detector (not shown) provided in the combustion section 50.

〈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、燃焼が開始された後は、燃焼部で
生じた高温排ガスによって空気を加熱することができる
ので、電気ヒータ使用による消費電力を減することがで
きる。また一般家庭において、電気ヒータ使用による電
気配線の容量の心配をすることなく使用することができ
る。さらに高温排ガスで直接的に空気を加熱するので、
燃料供給の急激な増加に伴う大量の加熱空気の供給に際
しても、素早く追従することかできる。
<Effects> The present invention has the above configuration, and according to the liquid fuel combustion device according to claim 1, after combustion is started, the air can be heated by the high temperature exhaust gas generated in the combustion section. , it is possible to reduce power consumption due to the use of electric heaters. Moreover, it can be used in a general household without worrying about the capacity of electric wiring due to the use of an electric heater. Furthermore, since the air is directly heated with high-temperature exhaust gas,
Even when a large amount of heated air is supplied due to a sudden increase in fuel supply, it can be quickly followed.

また請求項2に記載の液体燃料燃焼装置によれば、燃焼
の排熱が循環されることで、上記した請求項1の構成に
よる効果と同様な効果を得ることができる。しかも蒸発
室、燃焼部へは排ガスは混入されず、新鮮な空気だけが
供給されるので、燃焼効率もよい。
Further, according to the liquid fuel combustion apparatus according to the second aspect, the exhaust heat of combustion is circulated, so that it is possible to obtain the same effect as the above-mentioned effect obtained by the configuration according to the first aspect. Moreover, since no exhaust gas is mixed into the evaporation chamber or the combustion section, and only fresh air is supplied, combustion efficiency is also improved.

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

第1図は本発明の第1の実施例を示す断面構成図、第2
図は第1図のA−A断面図、第3図は本発明の第2の実
施例を示す断面構成図、第4図は第3図のB−B断面図
、第5図は従来装置の断面構成図、第6図は第5図のC 11:ファン 12:供給路 20:蒸発室 30:電気ヒータ 40:噴射ノズル 50:燃焼部 60:温度センサ 71:排ガス通路 72:制御弁 81:通路 82:制御弁 83:熱交換器 C断面図である。
FIG. 1 is a cross-sectional configuration diagram showing the first embodiment of the present invention, and FIG.
The figures are a cross-sectional view taken along the line AA in FIG. 1, FIG. 3 is a cross-sectional view showing the second embodiment of the present invention, FIG. 4 is a cross-sectional view taken along the line B-B in FIG. 3, and FIG. 5 is a conventional device. 11: Fan 12: Supply path 20: Evaporation chamber 30: Electric heater 40: Injection nozzle 50: Combustion section 60: Temperature sensor 71: Exhaust gas passage 72: Control valve 81 : Passage 82 : Control valve 83 : Heat exchanger C sectional view.

Claims (2)

【特許請求の範囲】[Claims] (1)、室内に導入された微粒化液体燃料を同じく室内
に導入された加熱空気で直接的に接触蒸発させる蒸発室
と、空気を外部から取り入れて前記蒸発室へ送り込む空
気送り込み手段と、外部から取り入れた空気を途中で加
熱するために設けられる電気的加熱手段と、液体燃料を
微粒化状態で前記蒸発室内に噴射する燃料導入手段と、
前記蒸発室で気化された燃料を燃焼させる燃焼部とを有
する液体燃料燃焼装置であって、前記燃焼部で生じた高
温排ガスの一部を前記取り入れられる空気に混合して循
環させる排ガス循環手段を設けたことを特徴とする液体
燃料燃焼装置。
(1) an evaporation chamber that directly evaporates the atomized liquid fuel introduced into the room with heated air also introduced into the room; an air feeding means that takes in air from the outside and sends it into the evaporation chamber; an electric heating means provided to heat the air taken in from the evaporation chamber midway, and a fuel introduction means for injecting liquid fuel in an atomized state into the evaporation chamber;
A liquid fuel combustion device comprising a combustion section that burns the fuel vaporized in the evaporation chamber, and an exhaust gas circulation means that mixes a part of the high-temperature exhaust gas generated in the combustion section with the air taken in and circulates the mixture. A liquid fuel combustion device characterized by:
(2)、排ガス循環手段を設ける代わりに、燃焼部で生
じた高温排熱を用いて送り込まれる空気を加熱する排熱
循環手段を設けたことを特徴とする請求項1に記載の液
体燃料燃焼装置。
(2) Liquid fuel combustion according to claim 1, characterized in that instead of providing the exhaust gas circulation means, an exhaust heat circulation means is provided that heats the air sent in using high temperature waste heat generated in the combustion section. Device.
JP17092190A 1990-06-27 1990-06-27 Liquid fuel burner Pending JPH0460307A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17092190A JPH0460307A (en) 1990-06-27 1990-06-27 Liquid fuel burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17092190A JPH0460307A (en) 1990-06-27 1990-06-27 Liquid fuel burner

Publications (1)

Publication Number Publication Date
JPH0460307A true JPH0460307A (en) 1992-02-26

Family

ID=15913824

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17092190A Pending JPH0460307A (en) 1990-06-27 1990-06-27 Liquid fuel burner

Country Status (1)

Country Link
JP (1) JPH0460307A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
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US8702420B2 (en) * 2004-12-08 2014-04-22 Lpp Combustion, Llc Method and apparatus for conditioning liquid hydrocarbon fuels

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JPS5730518B2 (en) * 1978-06-30 1982-06-29
JPH0282015A (en) * 1988-09-19 1990-03-22 Sanyo Electric Co Ltd Combustion control device for heater

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Publication number Priority date Publication date Assignee Title
JPS5730518B2 (en) * 1978-06-30 1982-06-29
JPH0282015A (en) * 1988-09-19 1990-03-22 Sanyo Electric Co Ltd Combustion control device for heater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8702420B2 (en) * 2004-12-08 2014-04-22 Lpp Combustion, Llc Method and apparatus for conditioning liquid hydrocarbon fuels
US9803854B2 (en) 2004-12-08 2017-10-31 Lpp Combustion, Llc. Method and apparatus for conditioning liquid hydrocarbon fuels

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