JP2001248808A - Combustion equipment - Google Patents

Combustion equipment

Info

Publication number
JP2001248808A
JP2001248808A JP2000059958A JP2000059958A JP2001248808A JP 2001248808 A JP2001248808 A JP 2001248808A JP 2000059958 A JP2000059958 A JP 2000059958A JP 2000059958 A JP2000059958 A JP 2000059958A JP 2001248808 A JP2001248808 A JP 2001248808A
Authority
JP
Japan
Prior art keywords
rich
light
premixed gas
flame
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
JP2000059958A
Other languages
Japanese (ja)
Inventor
Nobuhiko Fujiwara
宣彦 藤原
Yuko Kubota
勇幸 久保田
Norio Yotsuya
規夫 肆矢
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 JP2000059958A priority Critical patent/JP2001248808A/en
Publication of JP2001248808A publication Critical patent/JP2001248808A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To enable combustion equipment on the thick and thin fuel combustion method to obtain normal combustion by suppressing the recondensation of gasified liquid fuel. SOLUTION: In this combustion equipment, a thick-side opening 45 which enables a thick premixed gas generating chamber 39 to communicate with a thick burner port 23, a thin-side opening 46 which enables the chamber 39 to communicate with a thin premixed gas generating chamber 44, and the chamber 44 are provided in a heat transfer means 42 which returns the heat of flames to a gasifying means 37 and the recondensation of gasified fuel is prevented by suppressing the temperature drop of the fuel until the fuel reaches the burner ports 23 and 25. Therefore, the fuel can be burnt at a desired excess air ratio and the occurrence of NOx, CO, HC, soot, etc., can be suppressed. At the time of shutting-off this equipment, in addition, the occurrence of an offensive smell can be suppressed, because no condensed fuel is left.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は低NOx燃焼装置に
関するもので、特に濃淡燃焼方式に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low NOx combustion system, and more particularly to a lean combustion system.

【0002】[0002]

【従来の技術】従来の濃淡燃焼方式による燃焼装置は特
開平7−19419号公報に記載されているようなもの
が一般的であった。この燃焼装置は図5に示すように1
は燃焼管で、中央に混合室2、その両側に濃側炎口部3
を区画形成し、混合室2の上部に淡側炎口構成体4によ
り淡側炎口5を設けている。6は混合室2の下部に設け
た空気口、7は濃側炎口部3の内壁に設けた淡側ガス噴
出孔である。濃側炎口部3は上部に濃側炎口8、下部に
通孔9を設けた濃ガス室10を有する濃側炎口構成体1
1を装着して形成している。
2. Description of the Related Art Conventionally, a combustion apparatus based on a gray-scale combustion system has generally been described in JP-A-7-19419. As shown in FIG.
Is a combustion tube, in the center of which is a mixing chamber 2, and on both sides of it a dense flame port 3
And a light-side flame port 5 is provided at the upper part of the mixing chamber 2 by a light-side flame port structure 4. Reference numeral 6 denotes an air port provided in a lower portion of the mixing chamber 2, and 7 denotes a light-side gas ejection hole provided on an inner wall of the deep-side flame opening 3. The dense-side flame port 3 has a dense-gas chamber 10 provided with a dense-side flame port 8 in the upper part and a through hole 9 in the lower part.
1 is formed.

【0003】上記構成において、濃ガスは淡側ガス噴出
孔7から混合室2内に噴出し、空気口6からの空気と混
合して淡ガスを生成し、淡側炎口5から噴出燃焼して中
央部に淡火炎を形成する。一方通孔9から濃ガス室10
に流入した濃ガスは上部の濃側炎口8より噴出燃焼して
両側部に濃火炎を形成する。不安定な淡火炎は両側の濃
火炎によって保炎される。
In the above configuration, the rich gas is blown into the mixing chamber 2 from the light gas outlet 7 and mixed with the air from the air port 6 to generate a light gas. To form a light flame in the center. One-way hole 9 through dense gas chamber 10
The concentrated gas that has flowed into the blast blows out and burns from the upper dense side flame port 8 to form a rich flame on both sides. The unstable light flame is held by the rich flame on both sides.

【0004】ここで通孔9から濃ガス室10に流入する
濃ガスは通孔9の穴数または穴径で決定される開口面積
によりそのガス量が決まり、淡側ガス噴出口7から噴出
するガス量とガスの分配量が決定される。
Here, the amount of concentrated gas flowing into the dense gas chamber 10 from the through hole 9 is determined by the opening area determined by the number of holes or the hole diameter of the through hole 9, and is discharged from the light-side gas outlet 7. The gas amount and the gas distribution amount are determined.

【0005】[0005]

【発明が解決しようとする課題】しかしながら上記従来
の燃焼装置は、灯油等の液体燃料を加熱気化して燃焼さ
せる場合、淡側炎口5および濃側炎口8より上流部は低
温であり、気化燃料の温度が低下して凝縮し各部に付着
する。このため、再凝縮した燃料が気化した燃料に混じ
ってすすが発生したり、所望の空気過剰率で燃焼せずN
Ox、CO、HCが多く発生するなど正常な燃焼が得ら
れない課題があった。この現象はバーナの温度が低い着
火時において特に顕著である。また消火時においても凝
縮した燃料が残留して徐々に気化するため、強い臭気が
発生する課題もあった。
However, in the conventional combustion apparatus, when a liquid fuel such as kerosene is heated and vaporized and burned, the temperature upstream of the light-side flame port 5 and the deep-side flame port 8 is low. The temperature of the vaporized fuel drops and condenses and adheres to various parts. For this reason, the recondensed fuel mixes with the vaporized fuel to produce soot,
There is a problem that normal combustion cannot be obtained, such as generation of a large amount of Ox, CO, and HC. This phenomenon is particularly remarkable at the time of ignition when the burner temperature is low. Further, even during fire extinguishing, the condensed fuel remains and gradually evaporates, so that there is a problem that a strong odor is generated.

【0006】ここで通孔9を穿設した濃側炎口構成体1
1および淡側ガス噴出孔7を穿設した濃側炎口部3の上
流側は気化燃料の流れのよどみが生じ、この部分での再
凝縮が顕著である。また常温の空気を混合した淡ガスは
温度が下がり、混合室2の壁近傍を流れる淡ガスはさら
に温度が低下し、その部分での再凝縮も顕著である。
[0006] Here, the dark side flame port structure 1 having a through hole 9 formed therein
The stagnation of the flow of the vaporized fuel occurs on the upstream side of the dense-side flame port 3 in which the first gas injection hole 7 and the light-side gas ejection hole 7 are formed, and recondensation in this portion is remarkable. Further, the temperature of the fresh gas mixed with air at room temperature decreases, and the temperature of the fresh gas flowing near the wall of the mixing chamber 2 further decreases, and recondensation in that portion is also remarkable.

【0007】[0007]

【課題を解決するための手段】本発明は上記課題を解決
するため、淡予混合気生成室、濃予混合気生成室と濃炎
口とを連通させる濃側開口および濃予混合気生成室と淡
予混合気生成室とを連通させる淡側開口を火炎の熱を気
化手段に還流する伝熱手段に設けたものである。
SUMMARY OF THE INVENTION In order to solve the above problems, the present invention provides a lean premixed gas generation chamber, a rich premixed gas generation chamber, and a rich side opening and a rich premixed gas generation chamber communicating with the rich flame port. A light-side opening for communicating the gas with the light premixed gas generation chamber is provided in the heat transfer means for returning the heat of the flame to the vaporizing means.

【0008】上記発明によれば、濃炎口および淡炎口に
至るまでにおいて気化燃料の温度低下が抑制され、気化
燃料の再凝縮が防止される。よって所望の空気過剰率で
燃焼でき、NOx、CO、HC、すす等の発生を抑制す
ることができる。また消火時においても凝縮した燃料が
残留しないため臭気の発生を抑制することができる。
According to the invention, the temperature of the vaporized fuel is prevented from lowering down to the rich flame port and the light flame port, and recondensation of the vaporized fuel is prevented. Therefore, combustion can be performed at a desired excess air ratio, and generation of NOx, CO, HC, soot, and the like can be suppressed. Further, even when the fire is extinguished, the condensed fuel does not remain, so that generation of odor can be suppressed.

【0009】[0009]

【発明の実施の形態】本発明の請求項1にかかる燃焼装
置は、濃炎口および淡炎口と、火炎より受熱する受熱手
段と、前記受熱手段で受ける熱が還流され液体燃料を加
熱気化する気化手段と、前記受熱手段で受ける熱を前記
気化手段に還流する伝熱手段と、前記気化手段で気化し
た液体燃料と予混合用空気とを混合して濃予混合気を生
成する濃予混合気生成室と、前記伝熱手段に設け前記濃
予混合気と希釈用空気とを混合して淡予混合気を生成す
る淡予混合気生成室と、前記伝熱手段に設け前記濃予混
合気生成室と前記濃炎口とを連通させる濃側開口と、前
記伝熱手段に設け前記濃予混合気生成室と前記淡予混合
気生成室とを連通させる淡側開口とを備えている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A combustion apparatus according to a first aspect of the present invention includes a rich flame port and a light flame port, heat receiving means for receiving heat from a flame, and heat received by the heat receiving means being recirculated to heat and vaporize liquid fuel. Vaporizing means, heat transfer means for returning heat received by the heat receiving means to the vaporizing means, and a rich fuel mixture for mixing the liquid fuel vaporized by the vaporizing means and the premix air to produce a rich premixed gas. An air-fuel mixture generation chamber, a light-air-fuel mixture generation chamber provided in the heat transfer means for mixing the air-rich mixture and the dilution air to generate a light air-fuel mixture, and a rich air-fuel mixture generation chamber provided in the heat transfer means. A rich-side opening for communicating the mixture gas generation chamber with the rich flame port, and a light-side opening provided in the heat transfer means for communicating the rich premixture gas generation chamber and the light premixture gas generation chamber. I have.

【0010】そして、濃側開口、淡側開口および淡予混
合気生成室は燃焼熱が還流されて高温に維持される伝熱
手段に設けられているため、気化燃料が濃炎口および淡
炎口に至るまでに温度低下による再凝縮が発生しない。
よって所望の空気過剰率で燃焼でき、NOx、CO、H
C、すす等の発生を抑制することができる。また消火時
においても再凝縮した燃料が残留しないため臭気の発生
を抑制することができる。
Since the rich side opening, the light side opening and the light premixed gas generation chamber are provided in heat transfer means for returning the combustion heat to a high temperature, the vaporized fuel is supplied to the rich flame opening and the lean flame. No recondensation occurs due to the temperature drop to the mouth.
Therefore, combustion can be performed at a desired excess air ratio, and NOx, CO, H
C, soot, etc. can be suppressed from occurring. Further, even at the time of fire extinguishing, since the recondensed fuel does not remain, generation of odor can be suppressed.

【0011】本発明の請求項2にかかる燃焼装置は、希
釈用空気開口を伝熱手段に設けている。
In the combustion apparatus according to a second aspect of the present invention, the dilution air opening is provided in the heat transfer means.

【0012】そして、希釈用空気が伝熱手段を通流する
時に予熱されるため、淡予混合気の温度低下を抑制し、
淡予混合気生成室での気化燃料の再凝縮をさらに効果的
に抑制することができる。
Since the dilution air is preheated when flowing through the heat transfer means, a decrease in the temperature of the lean premixture is suppressed,
Recondensation of vaporized fuel in the lean premixed gas generation chamber can be more effectively suppressed.

【0013】本発明の請求項3にかかる燃焼装置は、濃
炎口および淡炎口は円周上に交互に配置され、前記濃炎
口および前記淡炎口に側面が対向する保炎筒を備え、前
記保炎筒を受熱手段としている。
According to a third aspect of the present invention, there is provided a combustion apparatus comprising a flame-holding cylinder in which a rich flame port and a light flame port are alternately arranged on a circumference, and a side surface of which faces the rich flame port and the light flame port. And the flame holding tube is used as a heat receiving means.

【0014】そして、濃火炎と淡火炎が受熱手段に衝突
し、効果的に受熱できるとともに、濃火炎と淡火炎のリ
フトを抑制できる。
Then, the rich flame and the light flame collide with the heat receiving means, so that the heat can be effectively received and the lift of the rich flame and the light flame can be suppressed.

【0015】本発明の請求項4にかかる燃焼装置は、濃
炎口および淡炎口は円周上に交互に配置され、前記濃炎
口および前記淡炎口に側面が対向する突起部を伝熱手段
に一体構成し、前記突起部を受熱手段としている。
In the combustion apparatus according to a fourth aspect of the present invention, the rich flame port and the light flame port are alternately arranged on the circumference, and the protruding portion whose side faces the rich flame port and the light flame port is transmitted. The projection is integrally formed with the heating means, and the projection is used as the heat receiving means.

【0016】そして、伝熱手段に一体構成された突起部
が受熱するため、伝熱手段を高温に維持でき、気化燃料
の再凝縮をさらに効果的に抑制することができる。
[0016] Since the projection integrally formed with the heat transfer means receives the heat, the heat transfer means can be maintained at a high temperature, and the recondensation of the vaporized fuel can be more effectively suppressed.

【0017】[0017]

【実施例】以下、本発明の実施例について図面を用いて
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0018】(実施例1)図1は本発明の実施例1にお
ける燃焼装置の断面図、図2(a)は同炎口板を示す平
面図、図2(b)は同隔壁板を示す平面図である。図3
は図1におけるA−A線断面図、図4は図1におけるB
−B線断面図である。
(Embodiment 1) FIG. 1 is a sectional view of a combustion apparatus according to Embodiment 1 of the present invention, FIG. 2 (a) is a plan view showing the flame port plate, and FIG. 2 (b) is a partition plate thereof. It is a top view. FIG.
FIG. 4 is a sectional view taken along line AA in FIG. 1, and FIG.
FIG. 4 is a cross-sectional view taken along line B.

【0019】図において、21は円板状の炎口板で、図
2(a)に示す通り第一の切り欠き22を濃予混合気が
噴出する濃炎口23とし、第二の切り欠き24を淡予混
合気が噴出する淡炎口25とし、かつ中央に第一の淡予
混合気通流開口26を有する。濃炎口23および淡炎口
25は円周上に交互に設けられる。第一の切り欠き22
は第二の切り欠き24よりも切り欠き幅を狭く、切り欠
き深さを浅くしている。27は円板状の隔壁板であり、
図2(b)に示す通り同心状に第一の濃予混合気通流開
口28を複数個設け、中央に第二の淡予混合気通流開口
29を設けている。隔壁板27は2枚の炎口板21を隔
てるものであり、第二の淡予混合気通路開口29の径は
第二の切り欠き24の終端が位置する径よりも大きく、
第一の切り欠き22の終端が位置する径よりも小さくし
ている。
In FIG. 2, reference numeral 21 denotes a disc-shaped flame opening plate. As shown in FIG. 2A, a first notch 22 is a dense flame outlet 23 from which a rich premixed gas is jetted, and a second notch is provided. Reference numeral 24 denotes a light flame port 25 through which a light premixed gas is jetted, and a first light premixed gas flow opening 26 is provided at the center. The rich flame ports 23 and the light flame ports 25 are provided alternately on the circumference. First notch 22
The width of the notch is smaller than that of the second notch 24, and the depth of the notch is shallower. 27 is a disk-shaped partition plate,
As shown in FIG. 2B, a plurality of first rich premixed gas flow openings 28 are provided concentrically, and a second light premixed gas flow opening 29 is provided at the center. The partition plate 27 separates the two flame opening plates 21, and the diameter of the second pale premixed gas passage opening 29 is larger than the diameter at which the end of the second notch 24 is located,
The diameter of the first notch 22 is smaller than the diameter at which the end of the first notch 22 is located.

【0020】30は底板であり、同心状に第二の濃予混
合気通流開口31を複数個設け、中央に第三の淡予混合
気通流開口32を設けている。底板30の上に前記隔壁
板27と炎口板21とを順次上下方向に重ねて積層配置
し、最後に天板33を設ける。炎口板21と隔壁板27
を一組とし、燃料入力によりこれらの組数を選択する。
Reference numeral 30 denotes a bottom plate, in which a plurality of second dense premixed gas flow openings 31 are provided concentrically, and a third light premixed gas flow opening 32 is provided in the center. The partition plate 27 and the flame port plate 21 are sequentially stacked on the bottom plate 30 in the vertical direction, and the top plate 33 is finally provided. Flame plate 21 and partition plate 27
Are set as one set, and the number of these sets is selected according to the fuel input.

【0021】ここで第一の切り欠き22の終端近傍、図
2に示した第一の濃予混合気通路28および図1に示し
た第二の濃予混合気通路31が重なり、濃予混合気の2
3への供給通路が形成される。一方図2に示した第一お
よび第二の淡予混合気通流開口26および29、図1に
示した第三の淡予混合気通流開口32が同心状に重な
り、淡予混合気の淡炎口25への供給通路が形成され
る。34および35は炎口板21に交互に形成される濃
火炎および淡火炎である。36は濃炎口23および淡炎
口25に側面が対向する保炎筒(受熱手段)である。
Here, near the end of the first notch 22, the first rich premixed gas passage 28 shown in FIG. 2 and the second rich premixed gas passage 31 shown in FIG. Ki 2
3 is formed. On the other hand, the first and second light premixed gas flow openings 26 and 29 shown in FIG. 2 and the third light premixed gas flow opening 32 shown in FIG. A supply passage to the light flame port 25 is formed. Numerals 34 and 35 denote a rich flame and a light flame alternately formed on the flame plate 21. Reference numeral 36 denotes a flame holding cylinder (heat receiving means) whose side faces face the rich flame port 23 and the light flame port 25.

【0022】37は液体燃料を加熱して気化する気化手
段であり、ヒータ38を内蔵している。気化手段37の
内部に濃予混合気生成室39が形成され、回転体40が
設けられている。41は液体燃料を供給するノズルであ
る。
Reference numeral 37 denotes vaporizing means for heating and vaporizing the liquid fuel, and includes a heater 38 therein. A rich premixed gas generation chamber 39 is formed inside the vaporizing means 37, and a rotating body 40 is provided. 41 is a nozzle for supplying liquid fuel.

【0023】42は気化手段37の下流に設けた伝熱手
段であり、伝熱手段42に濃炎口23および淡炎口25
に側面が対向する突起部43(受熱手段)を一体に構成
している。また伝熱手段42に淡予混合気が生成される
淡予混合気生成室44、濃予混合気生成室39と濃炎口
23とを連通させる濃側開口45、濃予混合気生成室3
9と淡予混合気生成室44とを連通させる淡側開口46
および希釈空気供給室47と淡予混合気生成室44とを
連通させる希釈用空気開口48を設けている。希釈用空
気開口48は図4に示すように所定間隔にて放射状に設
けられている。
Reference numeral 42 denotes a heat transfer means provided downstream of the vaporization means 37. The heat transfer means 42 is provided with a rich flame port 23 and a light flame port 25.
And a protrusion 43 (heat receiving means) whose side faces face each other. Further, a light premixed gas generation chamber 44 in which a light premixed gas is generated in the heat transfer means 42, a rich side opening 45 communicating the rich premixed gas generation chamber 39 with the rich flame port 23, and a rich premixed gas generation chamber 3
9 and a light-side opening 46 for communicating the light premixed gas generation chamber 44
In addition, a dilution air opening 48 for communicating the dilution air supply chamber 47 with the light premixed gas generation chamber 44 is provided. The dilution air openings 48 are provided radially at predetermined intervals as shown in FIG.

【0024】49は空気供給手段、50は濃予混合気生
成室39に連通する予混合用空気供給通路、51は希釈
用空気供給室47に連通する希釈用空気供給通路であ
る。
49 is an air supply means, 50 is a premixing air supply passage communicating with the rich premixed gas generation chamber 39, and 51 is a dilution air supply passage communicating with the dilution air supply chamber 47.

【0025】次に動作、作用について説明すると、図1
において、制御手段(図示せず)の着火指令信号により
ヒータ38に通電し気化手段37を所定の温度に予熱す
る。予熱終了後、液体燃料は燃料ポンプ(図示せず)に
よりノズル41により回転体40に供給される。回転体
40はモータ(図示せず)によって駆動され、遠心力で
回転体40より液体燃料を振切り微粒化する。微粒化し
た液体燃料は気化手段37の内側面に衝突し気化する。
Next, the operation and operation will be described.
In step (1), the heater 38 is energized by an ignition command signal from a control unit (not shown) to preheat the vaporizing unit 37 to a predetermined temperature. After the completion of the preheating, the liquid fuel is supplied to the rotating body 40 by the nozzle 41 by a fuel pump (not shown). The rotating body 40 is driven by a motor (not shown), and shakes and atomizes the liquid fuel from the rotating body 40 by centrifugal force. The atomized liquid fuel collides with the inner surface of the vaporizing means 37 and is vaporized.

【0026】空気供給手段49が供給する空気は二分割
され、一方は予混合用空気供給通路50を通流して濃予
混合気生成室39に予混合用空気として供給される。も
う一方は希釈用空気供給通路51を通流して希釈用空気
供給室47に供給される。濃予混合気は濃予混合気生成
室39において気化燃料と予混合用空気とが混合して生
成される。
The air supplied by the air supply means 49 is divided into two parts, one of which is supplied through the premixing air supply passage 50 to the rich premixed gas generation chamber 39 as premixing air. The other is supplied to the dilution air supply chamber 47 through the dilution air supply passage 51. The rich premixed gas is generated by mixing the vaporized fuel and the premixing air in the rich premixed gas generation chamber 39.

【0027】濃予混合気は伝熱手段42によって二系統
に分割される。濃予混合気の一部は濃側開口45を通流
し、濃炎口23に供給される。濃予混合気の残りは淡側
開口46を通流して淡予混合気生成室44に供給され、
希釈用空気開口48を通流して供給される希釈用空気に
よって希釈されて淡予混合気が生成される。淡予混合気
は淡予混合気生成室44から流出して、淡炎口25に供
給される。そして着火手段(図示せず)の動作により着
火し、濃火炎34および淡火炎35が形成される。着火
後、着火手段は動作を停止する。
The rich premixture is divided into two systems by the heat transfer means 42. Part of the rich premixed gas flows through the rich side opening 45 and is supplied to the rich flame outlet 23. The remainder of the rich premixed gas flows through the light side opening 46 and is supplied to the light premixed gas generation chamber 44,
It is diluted by the dilution air supplied through the dilution air opening 48 to produce a lean premix. The light premixed gas flows out of the light premixed gas generation chamber 44 and is supplied to the light flame port 25. Then, the flame is ignited by the operation of the ignition means (not shown), and a rich flame 34 and a light flame 35 are formed. After ignition, the ignition means stops operating.

【0028】濃火炎34および淡火炎35が円周上に交
互に形成されるので、濃火炎34および淡火炎35の配
列終端が存在しない。よって濃火炎34間あるいは淡火
炎35間で流速ばらつきが少なく均一で小分割された濃
火炎34および淡火炎35となり、流速過大による火炎
のリフト、あるいは流速過小による炎口板21の赤熱が
抑制される。また淡予混合気への燃料配分比率および空
気過剰率を増すことができ、NOxを抑制できる。
Since the rich flames 34 and the light flames 35 are alternately formed on the circumference, the arrangement end of the rich flames 34 and the light flames 35 does not exist. Accordingly, the flow velocity variation between the rich flames 34 or the light flames 35 is small, and the uniform flames are divided into the rich flames 34 and the light flames 35, which are small and uniform. You. Further, the fuel distribution ratio and the excess air ratio to the lean premix can be increased, and NOx can be suppressed.

【0029】濃火炎34、淡火炎35が保炎筒36およ
び突起部43に衝突し、リフトが効果的に抑制されると
ともに保炎筒36および突起部43が効率的に受熱し、
伝熱手段42により気化手段37に受熱が還流される。
着火してしばらくしてからヒータ38への通電は停止さ
れるが、気化手段37は所定温度(250℃)以上に維
持され液体燃料は気化される。
The rich flame 34 and the light flame 35 collide with the flame holding cylinder 36 and the projection 43, and the lift is effectively suppressed, and the flame holding cylinder 36 and the projection 43 receive heat efficiently.
The received heat is returned to the vaporizing means 37 by the heat transfer means 42.
After a while after the ignition, the power supply to the heater 38 is stopped, but the vaporizing means 37 is maintained at a predetermined temperature (250 ° C.) or higher, and the liquid fuel is vaporized.

【0030】ここで淡予混合気生成室44、濃側開口4
5および淡側開口46は保炎筒36および突起部43の
受熱により高温に維持される伝熱手段42に設けられて
いるため、濃予混合気および淡予混合気は濃炎口23お
よび淡炎口25に至る経路で温度低下による再凝縮が発
生しない。さらに希釈用空気は希釈用空気開口48を通
流する際に伝熱手段42により予熱されるため、濃予混
合気に低温である希釈用空気を混合して淡予混合気を生
成しても淡予混合気は再凝縮以上の温度に維持される。
よって所望の空気過剰率で燃焼でき、NOx、CO、H
C、すす等の発生を抑制することができる。また消火時
においても凝縮した燃料が残留しないため臭気の発生を
抑制することができる。
Here, the light premixed gas generation chamber 44 and the dense side opening 4
5 and the light side opening 46 are provided in the heat transfer means 42 which is maintained at a high temperature by the heat received by the flame holding cylinder 36 and the projection 43, so that the rich premixed gas and the light premixed gas are supplied to the rich flame port 23 and the light No recondensation occurs due to a temperature drop in the path leading to the flame outlet 25. Further, since the dilution air is preheated by the heat transfer means 42 when flowing through the dilution air opening 48, even if the rich premixed air is mixed with the low-temperature dilution air to produce a light premixed air. The light premix is maintained at a temperature above the recondensation.
Therefore, combustion can be performed at a desired excess air ratio, and NOx, CO, H
C, soot and the like can be suppressed. Further, even when the fire is extinguished, the condensed fuel does not remain, so that generation of odor can be suppressed.

【0031】なお、前記実施例において都市ガス等の気
体燃料を用いることもできる。その場合、上記実施例で
説明した液体燃料の気化に関係する構成は省略できる。
In the above embodiment, gaseous fuel such as city gas can be used. In that case, the configuration related to the vaporization of the liquid fuel described in the above embodiment can be omitted.

【0032】[0032]

【発明の効果】以上説明したように請求項1に係る発明
は、濃側開口、淡側開口および淡予混合気生成室は燃焼
熱が還流されて高温に維持される伝熱手段に設けられて
いるため、気化燃料が濃炎口および淡炎口に至るまでに
温度低下による再凝縮が発生しない。よって所望の空気
過剰率で燃焼でき、NOx、CO、HC、すす等の発生
を抑制することができる。また消火時においても再凝縮
した燃料が残留しないため臭気の発生を抑制することが
できる。
As described above, according to the first aspect of the present invention, the rich side opening, the light side opening and the light premixed gas generation chamber are provided in the heat transfer means in which the combustion heat is recirculated and maintained at a high temperature. Therefore, recondensation due to a temperature drop does not occur before the vaporized fuel reaches the rich flame port and the light flame port. Therefore, combustion can be performed at a desired excess air ratio, and generation of NOx, CO, HC, soot, and the like can be suppressed. Further, even at the time of fire extinguishing, since the recondensed fuel does not remain, generation of odor can be suppressed.

【0033】また、請求項2に係る発明は、希釈用空気
が伝熱手段を通流する時に予熱されるため、淡予混合気
の温度低下を抑制し、淡予混合気生成室での気化燃料の
再凝縮をさらに効果的に抑制することができる。
According to the second aspect of the present invention, since the dilution air is preheated when flowing through the heat transfer means, a decrease in the temperature of the lean premixture is suppressed, and the vaporization in the lean premixture generation chamber is performed. Fuel recondensation can be more effectively suppressed.

【0034】また、請求項3に係る発明は、濃火炎と淡
火炎が受熱手段に衝突し、効果的に受熱できるととも
に、濃火炎と淡火炎のリフトを抑制できる。
Further, according to the third aspect of the present invention, the rich flame and the light flame collide with the heat receiving means, so that the heat can be effectively received and the lift of the rich flame and the light flame can be suppressed.

【0035】また、請求項4に係る発明は、伝熱手段に
一体構成された突起部が受熱するため、伝熱手段を高温
に維持でき、気化燃料の再凝縮をさらに効果的に抑制す
ることができる。
According to the fourth aspect of the present invention, since the projection integrated with the heat transfer means receives heat, the heat transfer means can be maintained at a high temperature, and the recondensation of the vaporized fuel can be more effectively suppressed. Can be.

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

【図1】本発明の一実施例における燃焼装置の断面図
(図3および図4におけるX−Y−Z線断面図)
FIG. 1 is a sectional view of a combustion device according to an embodiment of the present invention (a sectional view taken along line XYZ in FIGS. 3 and 4).

【図2】(a)同燃焼装置の炎口板を示す平面図 (b)同燃焼装置の隔壁板を示す平面図FIG. 2A is a plan view showing a flame port plate of the combustion device. FIG. 2B is a plan view showing a partition plate of the combustion device.

【図3】同燃焼装置の図1におけるA−A線断面図FIG. 3 is a sectional view of the combustion device taken along line AA in FIG. 1;

【図4】同燃焼装置の図1におけるB−B線断面図FIG. 4 is a sectional view of the combustion device taken along line BB in FIG. 1;

【図5】従来の燃焼装置を示す斜視図FIG. 5 is a perspective view showing a conventional combustion device.

【符号の説明】[Explanation of symbols]

23 濃炎口 25 淡炎口 36 保炎筒(受熱手段) 37 気化手段 39 濃予混合気生成室 42 伝熱手段 43 突起部(受熱手段) 44 淡予混合気生成室 45 濃側開口 46 淡側開口 48 希釈用空気開口 23 Rich Flame Port 25 Light Flame Port 36 Flame Holding Cylinder (Heat Receiving Means) 37 Evaporating Means 39 Rich Premixed Gas Generation Chamber 42 Heat Transfer Means 43 Projection (Heat Receiving Means) 44 Light Premixed Gas Generation Chamber 45 Dark Side Opening 46 Light Side opening 48 Air opening for dilution

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23D 11/44 F23D 11/44 B (72)発明者 肆矢 規夫 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 3K052 AA05 AC01 EB07 EB09 3K065 TA01 TA04 TD04 TH04 TP01──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) F23D 11/44 F23D 11/44 B (72) Inventor Norio Shiya 1006 Odakadoma, Kadoma City, Osaka Matsushita Electric Industrial F term in the company (reference) 3K052 AA05 AC01 EB07 EB09 3K065 TA01 TA04 TD04 TH04 TP01

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】濃炎口および淡炎口と、火炎より受熱する
受熱手段と、前記受熱手段で受ける熱が還流され液体燃
料を加熱気化する気化手段と、前記受熱手段で受ける熱
を前記気化手段に還流する伝熱手段と、前記気化手段で
気化した液体燃料と予混合用空気とを混合して濃予混合
気を生成する濃予混合気生成室と、前記伝熱手段に設け
前記濃予混合気と希釈用空気とを混合して淡予混合気を
生成する淡予混合気生成室と、前記伝熱手段に設け前記
濃予混合気生成室と前記濃炎口とを連通させる濃側開口
と、前記伝熱手段に設け前記濃予混合気生成室と前記淡
予混合気生成室とを連通させる淡側開口とを備えた燃焼
装置。
A heat receiving means for receiving heat from the flame; a heat receiving means for receiving heat from the flame; a vaporizing means for heating and vaporizing the liquid fuel by recirculating heat received by the heat receiving means; A heat transfer means for returning to the means, a rich premixed gas generation chamber for mixing the liquid fuel vaporized by the vaporizing means with the premixing air to generate a rich premixed gas, and the rich heat transfer means provided in the heat transfer means. A light premixed gas generation chamber for mixing the premixed gas and the dilution air to generate a light premixed gas; and a rich gas mixture chamber provided in the heat transfer means and communicating with the rich premixed gas generation chamber and the rich flame port. A combustion device comprising: a side opening; and a light-side opening provided in the heat transfer means and communicating the rich premixed gas generation chamber and the light premixed gas generation chamber.
【請求項2】希釈用空気開口を伝熱手段に設けた請求項
1記載の燃焼装置。
2. The combustion apparatus according to claim 1, wherein an air opening for dilution is provided in the heat transfer means.
【請求項3】濃炎口および淡炎口は円周上に交互に配置
され、前記濃炎口および前記淡炎口に側面が対向する保
炎筒を備え、前記保炎筒を受熱手段とする請求項1ない
し2のいずれか1項記載の燃焼装置。
3. A rich flame port and a light flame port are alternately arranged on a circumference, and a flame holding cylinder whose side faces the rich flame port and the light flame port is provided. The combustion device according to claim 1, wherein
【請求項4】濃炎口および淡炎口は円周上に交互に配置
され、前記濃炎口および前記淡炎口に側面が対向する突
起部を伝熱手段に一体構成し、前記突起部を受熱手段と
する請求項1ないし3のいずれか1項記載の燃焼装置。
4. A rich flame port and a light flame port are alternately arranged on a circumference, and a projection having a side surface facing the rich flame port and the light flame port is integrally formed with a heat transfer means. The combustion device according to any one of claims 1 to 3, wherein the device is a heat receiving unit.
JP2000059958A 2000-03-06 2000-03-06 Combustion equipment Pending JP2001248808A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000059958A JP2001248808A (en) 2000-03-06 2000-03-06 Combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000059958A JP2001248808A (en) 2000-03-06 2000-03-06 Combustion equipment

Publications (1)

Publication Number Publication Date
JP2001248808A true JP2001248808A (en) 2001-09-14

Family

ID=18580345

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000059958A Pending JP2001248808A (en) 2000-03-06 2000-03-06 Combustion equipment

Country Status (1)

Country Link
JP (1) JP2001248808A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103471096A (en) * 2012-06-08 2013-12-25 佛山市源威科技开发有限公司 Biological alcohol oil combustion device
CN108662768A (en) * 2017-04-01 2018-10-16 芜湖美的厨卫电器制造有限公司 Positive displacement heat-exchanger rig and water heater with it

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103471096A (en) * 2012-06-08 2013-12-25 佛山市源威科技开发有限公司 Biological alcohol oil combustion device
CN103471096B (en) * 2012-06-08 2016-04-20 佛山市源威科技开发有限公司 A kind of biological alcohol oil combustion device
CN108662768A (en) * 2017-04-01 2018-10-16 芜湖美的厨卫电器制造有限公司 Positive displacement heat-exchanger rig and water heater with it
CN108662768B (en) * 2017-04-01 2023-11-14 芜湖美的厨卫电器制造有限公司 Volumetric heat exchange device and water heater with same

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