JPH05203118A - Combustion equipment - Google Patents

Combustion equipment

Info

Publication number
JPH05203118A
JPH05203118A JP3876492A JP3876492A JPH05203118A JP H05203118 A JPH05203118 A JP H05203118A JP 3876492 A JP3876492 A JP 3876492A JP 3876492 A JP3876492 A JP 3876492A JP H05203118 A JPH05203118 A JP H05203118A
Authority
JP
Japan
Prior art keywords
fuel
combustion
heating
air
catalyst
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
JP3876492A
Other languages
Japanese (ja)
Inventor
Takahiro Matsuda
孝洋 松田
Kosaku Shirode
浩作 城出
Toshio Watanabe
俊雄 渡辺
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 JP3876492A priority Critical patent/JPH05203118A/en
Publication of JPH05203118A publication Critical patent/JPH05203118A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain a combustion equipment which does not require a blower having a large capacity, restrains the generation of tar, prevents the reliquefaction of gaseous fuel, can stably burn with the catalyst at a temperature lower than that for the burning catalyst to be durable, causes low pollution and low noise, can be compactly constituted. CONSTITUTION:A combustion equipment has a blowing means 51, a heating means 61 for heating air from the blowing means 51, a heating vaporization means 52 for liquid fuel, a spray supply means 53 for fuel vaporized by the heating vaporization means 52. While mixing vaporized fuel sprayed from the spray supply means 53 with high temperature air obtained in the heating means 61, the burning catalyst is supplied to a porous burning plate 54 carrying the burning catalyst to burn it.

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用
い、燃焼触媒を利用して触媒燃焼させる燃焼装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion apparatus which uses a liquid fuel such as kerosene and uses a combustion catalyst for catalytic combustion.

【0002】[0002]

【従来の技術】図4に従来の燃焼装置の断面構成図を示
す。この従来装置は、電熱による燃料加熱気化器52と燃
料噴霧ノズル53を持ち、送風器51による常温空気と、前
記燃料噴霧ノズル53からの高温の燃料蒸気とを混合する
構造を有し、また燃焼触媒を担持したセラミックス等の
多孔質燃焼板54に前記燃焼触媒の予熱のための触媒層加
熱器55と、その上部にフィン59を取り付けた水管58を有
し、循環する水を加熱することができようにされてい
る。液体燃料は前記燃料加熱気化器52で加熱気化され、
蒸気となってノズル53より噴出し、送風器51からの常温
空気と混合されながら多孔質燃焼板54に供給され、触媒
燃焼する。燃焼によって生じた高温ガスは、フィン59を
介して水管53内の水と熱交換する。
2. Description of the Related Art FIG. 4 is a sectional view showing the structure of a conventional combustion apparatus. This conventional device has a fuel heating vaporizer 52 by electric heat and a fuel spray nozzle 53, and has a structure for mixing room temperature air by a blower 51 and high-temperature fuel vapor from the fuel spray nozzle 53, and burning. A porous combustion plate 54 such as a ceramic carrying a catalyst has a catalyst layer heater 55 for preheating the combustion catalyst, and a water pipe 58 having fins 59 attached to the upper portion thereof to heat circulating water. It is possible. The liquid fuel is heated and vaporized by the fuel heating vaporizer 52,
It becomes steam and is ejected from the nozzle 53, supplied to the porous combustion plate 54 while being mixed with room temperature air from the blower 51, and undergoes catalytic combustion. The high temperature gas generated by the combustion exchanges heat with the water in the water pipe 53 via the fins 59.

【0003】[0003]

【発明が解決しようとする課題】ところが上記従来装置
では、 .多孔質燃焼板54の触媒層の温度をその耐久温度以下
にするため、送風器51の送風量は理論空気量の4倍程度
以上として混合気の透過率を大きくする必要があり、大
能力の送風器が必要である。 .大量の空気と混合しても再液化しないためには、燃
料加熱気化器52による温度を高温にし、ノズル53より噴
出する蒸気温度を上げることが必要であるが、それによ
りタールが発生してノズル53が詰まる欠点がある。 .大量の低温の空気と気化燃料とが混合するため、気
化燃料の再液化現象がどうしても生じる欠点があり、し
かも多孔質燃焼板54に再液化した液体燃料が再度加熱分
解され、触媒層の表面にタールが付着して触媒の活性を
消失させる欠点がある。 .運転開始時に多孔質板54の触媒層の温度を触媒活性
可能な温度に上昇させるための手段、即ち触媒層加熱器
55が、前記燃料加熱気化器52の他に必要であった。また
従来の触媒層加熱器55では触媒層を均一に予熱すること
が出来なかった。
However, in the above conventional device, In order to keep the temperature of the catalyst layer of the porous combustion plate 54 below its endurance temperature, it is necessary to increase the air permeability of the air blower 51 to at least four times the theoretical air amount to increase the permeability of the air-fuel mixture. You need a blower. . In order to prevent re-liquefaction even when mixed with a large amount of air, it is necessary to raise the temperature by the fuel heating vaporizer 52 and raise the temperature of the steam ejected from the nozzle 53. There is a drawback that 53 is blocked. . Since a large amount of low-temperature air and vaporized fuel are mixed, there is a drawback that vaporized fuel reliquefaction phenomenon is inevitable, and the liquid fuel reliquefied to the porous combustion plate 54 is again decomposed by heating, and it becomes There is a drawback that tar adheres and the activity of the catalyst disappears. . Means for raising the temperature of the catalyst layer of the porous plate 54 to a temperature at which the catalyst can be activated at the start of operation, that is, a catalyst layer heater
55 was required in addition to the fuel heating vaporizer 52. Further, the conventional catalyst layer heater 55 cannot uniformly preheat the catalyst layer.

【0004】そこで、本発明は上記従来技術の欠点を解
消し、大能力の送風器を必要とせず、タールの発生を抑
え、気化燃料の再液化を防止し、燃焼触媒の耐久温度以
下で安定して触媒燃焼でき、低公害、低騒音で、コンパ
クトに構成できる燃焼装置の提供を目的とする。
Therefore, the present invention solves the above-mentioned drawbacks of the prior art, does not require a blower with a large capacity, suppresses the generation of tar, prevents the reliquefaction of vaporized fuel, and is stable below the endurance temperature of the combustion catalyst. It is an object of the present invention to provide a combustion device that can be catalytically burned, has low pollution and noise, and can be configured compactly.

【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、本発明の燃焼装置は、送風手段と、該送風手段から
の空気を加熱する加熱手段と、液体燃料の加熱気化手段
と、該加熱気化手段により蒸気化した燃料の噴霧供給手
段とを有し、前記噴霧供給手段により噴霧した蒸気化燃
料に前記加熱手段で得た高温空気を混合しながら、燃焼
触媒を担持した多孔質燃焼板に供給して燃焼させること
を第1の特徴としている。また本発明の燃焼装置は、前
記第1の特徴に加えて、送風手段と、該送風手段からの
空気を加熱する加熱手段と、液体燃料の噴霧供給手段
と、前記送風手段から加熱手段を経て送り込まれる高温
空気と前記噴霧供給手段から吹き込まれた噴霧燃料とを
直接的に接触させて気化する気化室とを有し、気化室か
ら送られてくる混合気を燃焼触媒を担持した多孔質燃焼
板で燃焼させることを第2の特徴としている。
In order to achieve the above object, the combustion apparatus of the present invention comprises a blowing means, a heating means for heating the air from the blowing means, a heating vaporization means for liquid fuel, and the heating means. A spray supply means for the fuel vaporized by the vaporization means, while mixing the vaporized fuel sprayed by the spray supply means with the high-temperature air obtained by the heating means, to a porous combustion plate carrying a combustion catalyst. The first feature is to supply and burn. Further, in addition to the first feature, the combustion apparatus of the present invention further includes a blowing unit, a heating unit that heats air from the blowing unit, a liquid fuel spray supply unit, and a heating unit that blows air from the blowing unit. Porous combustion that has a vaporization chamber that directly vaporizes by direct contact between the high-temperature air that is sent in and the spray fuel that is blown from the spray supply means, and the air-fuel mixture that is sent from the vaporization chamber carries a combustion catalyst. The second feature is to burn with a plate.

【0006】[0006]

【作用】上記第1の特徴によれば、送風手段からの空気
が加熱されて、高温空気となっ供給される。また液体燃
料は燃料加熱気化器52で加熱蒸気化され、供給される。
そして燃料蒸気と高温空気とが混合されながら燃焼触媒
担持の多孔質燃焼板に供給されて、触媒燃焼される。噴
霧された蒸気燃料は高温空気と混合されるので、常温空
気と混合させる場合よりも従来の燃料加熱気化器52によ
る燃料加熱温度を低くできるため、タールの発生が防止
され、燃料噴霧ノズルが詰まるのが防止される。また蒸
気燃料が高温空気と混合されるので、蒸気燃料の再液化
が抑制され、多孔質燃焼板にタールが付着するのが防止
される。また高温空気により多孔質燃焼板の燃焼触媒が
予備加熱されるので、従来の触媒層加熱器55が不必要と
なり、また均一加熱ができ、触媒燃焼が安定して行え
る。また多孔質燃焼板の燃焼触媒を耐久温度以下に調整
し易く、また予熱時間も大幅に短縮できる。また上記第
2の特徴によれば、送風手段からの空気が加熱されて、
高温空気となって気化室に送り込まれ、また噴霧供給手
段から液体燃料が気化室に噴霧供給され、この噴霧液体
燃料が前記高温空気と気化室内で直接的に接触して、混
合気化される。そして気化室で充分混合された混合気
が、燃焼触媒担持の多孔質燃焼板に供給されて、触媒燃
焼される。気化室で充分に混合気化された混合気が燃焼
に供されるので、燃焼が一層安定する。噴霧燃料を気化
室内で高温空気により直接的に且つ充分に接触して蒸発
気化できるので、従来の燃料加熱気化器52を不要とする
ことができる。よって燃料噴霧ノズルにタールが詰まる
といったこともない。また直接接触により燃料が効率よ
く気化されるので、高温空気の温度自体はタールが生じ
る温度よりも充分に低く設定でき、空気加熱手段の必要
電力等も低く抑えることができる。また高温空気により
多孔質燃焼板の燃焼触媒が予備加熱されるので、従来の
触媒層加熱器55が不必要となり、また均一加熱ができ、
触媒燃焼が安定して行える。また多孔質燃焼板の燃焼触
媒を耐久温度以下に調整し易く、また予熱時間も大幅に
短縮できる。
According to the first feature, the air from the blowing means is heated and supplied as high temperature air. The liquid fuel is heated and vaporized by the fuel heating vaporizer 52 and supplied.
Then, the fuel vapor and the high temperature air are mixed and supplied to the porous combustion plate supporting the combustion catalyst to be catalytically combusted. Since the atomized vapor fuel is mixed with high temperature air, the fuel heating temperature by the conventional fuel heating vaporizer 52 can be made lower than in the case of being mixed with room temperature air, so that the generation of tar is prevented and the fuel spray nozzle is clogged. Is prevented. Further, since the steam fuel is mixed with the high temperature air, reliquefaction of the steam fuel is suppressed and tar is prevented from adhering to the porous combustion plate. Further, since the combustion catalyst of the porous combustion plate is preheated by the high temperature air, the conventional catalyst bed heater 55 is unnecessary, and uniform heating can be performed, so that the catalytic combustion can be stably performed. Further, it is easy to adjust the combustion catalyst of the porous combustion plate to a temperature not higher than the durability temperature, and the preheating time can be shortened significantly. Further, according to the second feature, the air from the blowing means is heated,
High-temperature air is sent to the vaporization chamber, and liquid fuel is spray-supplied from the spray supply means to the vaporization chamber, and the sprayed liquid fuel directly contacts the high-temperature air in the vaporization chamber and is mixed and vaporized. Then, the air-fuel mixture that has been sufficiently mixed in the vaporization chamber is supplied to the porous combustion plate carrying the combustion catalyst to be catalytically combusted. Since the air-fuel mixture sufficiently mixed and vaporized in the vaporization chamber is used for combustion, the combustion is further stabilized. Since the atomized fuel can be directly and sufficiently contacted with the hot air in the vaporization chamber to be vaporized and vaporized, the conventional fuel heating vaporizer 52 can be omitted. Therefore, the fuel spray nozzle is not clogged with tar. Further, since the fuel is efficiently vaporized by direct contact, the temperature itself of the high temperature air can be set sufficiently lower than the temperature at which tar is generated, and the power required by the air heating means and the like can be kept low. Further, since the combustion catalyst of the porous combustion plate is preheated by the high temperature air, the conventional catalyst layer heater 55 is unnecessary, and uniform heating is possible.
Catalytic combustion can be performed stably. Further, it is easy to adjust the combustion catalyst of the porous combustion plate to a temperature not higher than the durability temperature, and the preheating time can be shortened significantly.

【0007】[0007]

【実施例】図1は本発明装置の第1の実施例を示す燃焼
装置の全体の断面構成図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a sectional view of the whole combustion apparatus showing a first embodiment of the apparatus of the present invention.

【0008】液体燃料の加熱気化手段として電熱による
燃料加熱気化器52を持ち、燃料の噴霧供給手段として燃
料噴霧ノズル53を持ち、また送風手段として送風器51に
より空気を送る点、及び燃焼触媒を担持したセラミック
ス等の多孔質燃焼板54とその上方にフィン59を取り付け
た水管58を設け、循環する水を加熱することができるよ
うにした点は従来と同様である。本装置では、前記送風
器51の下流に空気加熱手段として空気加熱器61を設け、
送風器51からの空気を高温に加熱するようにしている。
そして多孔質燃焼板54の燃焼触媒を予熱するために従来
用いていた触媒層加熱器は設けない。送風器51によって
供給された空気は電熱による空気加熱器61で高温に加熱
され、触媒を担持した多孔質燃焼板54を燃焼触媒が活性
を示す温度まで加熱する。高温空気により多孔質燃焼板
54全体を均一に加熱するため、従来より予熱の時間が大
幅に短縮でき、また燃焼が安定する。更に燃焼触媒層を
耐久温度以下に調整燃焼がし易い。また噴霧ノズル53か
らの噴霧蒸気は常温空気でなく高温空気と混合されるの
で、燃料加熱気化器52による温度はタールが生じる温度
よりも充分低くしても、噴霧蒸気が再液化することがな
い。よってノズル53詰まりがなくなる。更に噴霧ノズル
より噴出した燃料蒸気の気化が不充分であっても、高温
空気により気化が更に進むため、触媒層に液滴のまま燃
料が供給されることがない。なお、燃焼は多孔質燃焼板
54の燃焼触媒層で完結するため、フィン59付水管58との
距離Lは殆ど必要なく、燃焼空間は殆ど不要である。
A fuel heating vaporizer 52 by electric heat is provided as a heating vaporization means for liquid fuel, a fuel spray nozzle 53 is provided as a fuel spray supply means, and a point for sending air by a blower 51 as a blower means and a combustion catalyst. As in the prior art, a porous combustion plate 54 made of ceramics and the like and a water pipe 58 having fins 59 attached above it were provided so that the circulating water could be heated. In this device, an air heater 61 is provided as air heating means downstream of the blower 51,
The air from the blower 51 is heated to a high temperature.
The catalyst bed heater conventionally used for preheating the combustion catalyst of the porous combustion plate 54 is not provided. The air supplied by the blower 51 is heated to a high temperature by the air heater 61 by electric heat, and heats the catalyst-supporting porous combustion plate 54 to a temperature at which the combustion catalyst is active. Porous combustion plate with hot air
Since the whole 54 is heated uniformly, the preheating time can be greatly shortened compared with the conventional one, and the combustion becomes stable. Furthermore, the combustion of the combustion catalyst layer is easily adjusted and burned to a temperature not higher than the endurance temperature. Further, since the spray vapor from the spray nozzle 53 is mixed with high temperature air instead of room temperature air, the spray vapor does not reliquefy even if the temperature by the fuel heating vaporizer 52 is sufficiently lower than the temperature at which tar is generated. . Therefore, the nozzle 53 is not clogged. Further, even if the vaporization of the fuel vapor ejected from the atomizing nozzle is insufficient, the vaporization is further promoted by the high temperature air, so that the fuel is not supplied as droplets to the catalyst layer. In addition, combustion is a porous combustion plate
Since it is completed with the combustion catalyst layer 54, the distance L to the water pipe 58 with the fin 59 is hardly necessary, and the combustion space is almost unnecessary.

【0009】図2は本発明装置の第2の実施例を示す燃
焼装置の全体の断面構成図で、図3は気化室を横からみ
た断面図である。
FIG. 2 is a sectional view of the entire combustion apparatus showing a second embodiment of the apparatus of the present invention, and FIG. 3 is a sectional view of the vaporization chamber as seen from the side.

【0010】送風手段である送風器51からの送風路62
に、空気の加熱手段たる空気加熱器61を設け、前記送風
路62の高温空気送込口63を、横置きの円筒状に構成した
気化容器65の側壁に対して接線方向に接続している。そ
してまた燃料の噴霧供給手段である燃料噴霧ノズル53
を、前記気化容器65の中心軸上を前記送込口63のある側
とは遠い方の端壁から気化室66内に臨ませている。また
気化容器65からの送出口67も容器側壁から接線方向に設
けられている。前記空気加熱器61は電熱による加熱器と
することができる。燃料噴霧ノズル53の手前には液体燃
料の加熱気化器は設けない。多孔質燃焼板54、水管58、
フィン59の構成は上記第1の実施例と同じである。
An air passage 62 from an air blower 51, which is an air blower.
An air heater 61 is provided as a means for heating the air, and the high temperature air inlet 63 of the air passage 62 is tangentially connected to the side wall of the horizontally arranged cylindrical vaporization container 65. .. And again, the fuel spray nozzle 53 which is a fuel spray supply means.
Is exposed to the inside of the vaporization chamber 66 from the end wall on the central axis of the vaporization container 65, which is far from the side where the feed port 63 is located. A delivery port 67 from the vaporization container 65 is also provided in a tangential direction from the container side wall. The air heater 61 may be an electric heater. A liquid fuel heating vaporizer is not provided in front of the fuel spray nozzle 53. Porous combustion plate 54, water pipe 58,
The structure of the fin 59 is the same as that of the first embodiment.

【0011】しかして、送風器51によって供給された空
気は空気加熱器61で高温に加熱され、円筒状の気化容器
65を通って触媒を担持した多孔質燃焼板54に供給され、
燃焼触媒層を触媒反応が可能な温度まで予熱する。高温
空気は多孔質燃焼板54全体を均一に加熱するため、従来
より予熱の時間を大幅に短縮できる。液体燃料の噴霧ノ
ズル53より気化室66内に微粉化状態で液体燃料を供給す
ることにより、該微粉化液体燃料が前記高温空気によっ
て直接的に接触加熱され、気化される。直接接触による
気化であるので、前記高温空気の温度は比較的低く設定
しても気化を行うことができるので、タールの発生をな
くすることができる。また空気加熱器61の必要電力も低
く抑えることができる。勿論気化室66で充分に気化が行
われるので、液体燃料の加熱気化器は不要であり、ノズ
ル53がタール詰まりすることもない。前記気化室66内
で、気化された燃料は高温空気と充分に混合され、混合
気となって多孔質燃焼板54へ送られ、担持された燃焼触
媒層上で燃焼する。気化室66で充分に混合された混合気
による燃焼であるので、上記第1の実施例の場合よりも
一層燃焼が安定する。勿論燃焼は触媒燃焼であるので、
NO2 等は発生しない。
The air supplied by the blower 51 is heated to a high temperature by the air heater 61, and the cylindrical vaporization container
It is supplied to the porous combustion plate 54 supporting the catalyst through 65,
The combustion catalyst layer is preheated to a temperature at which the catalytic reaction is possible. Since the high temperature air uniformly heats the entire porous combustion plate 54, the preheating time can be greatly shortened as compared with the conventional case. By supplying the liquid fuel into the vaporization chamber 66 from the liquid fuel spray nozzle 53 in a finely divided state, the finely divided liquid fuel is directly contact-heated by the high temperature air and vaporized. Since vaporization is performed by direct contact, vaporization can be performed even if the temperature of the high temperature air is set to be relatively low, and thus tar can be eliminated. In addition, the electric power required for the air heater 61 can be kept low. Of course, since vaporization is sufficiently carried out in the vaporization chamber 66, a heating vaporizer for liquid fuel is unnecessary, and the nozzle 53 is not clogged with tar. In the vaporization chamber 66, the vaporized fuel is sufficiently mixed with high temperature air to form a mixture, which is sent to the porous combustion plate 54 and burned on the supported combustion catalyst layer. Since the combustion is performed by the air-fuel mixture that is sufficiently mixed in the vaporization chamber 66, the combustion is more stable than in the case of the first embodiment. Of course, combustion is catalytic combustion, so
NO 2 etc. do not occur.

【0012】[0012]

【発明の効果】本発明は以上の構成、作用よりなり、請
求項1に記載の燃焼装置によれば、噴霧された蒸気燃料
を高温空気と混合するので、常温空気と混合させる場合
よりも燃料加熱気化器による燃料加熱温度を低くできる
ため、タールの発生を防止でき、燃料噴霧ノズルが詰ま
るのが防止できる。また蒸気燃料を高温空気と混合する
ので、蒸気燃料の再液化を抑制でき、多孔質燃焼板にタ
ールが付着するのが防止できる。また高温空気により多
孔質燃焼板の燃焼触媒を予備加熱するので、触媒層加熱
器が不必要となり、また均一加熱ができ、触媒燃焼が安
定して行える。また多孔質燃焼板の燃焼触媒を耐久温度
以下に調整し易く、また予熱時間も大幅に短縮できる。
また請求項2の燃焼装置によれば、気化室で充分に混合
気化した混合気を燃焼に供するので、燃焼を一層安定さ
せることができる。噴霧燃料を気化室内で高温空気によ
り直接的に且つ充分に接触して蒸発気化できるので、従
来の燃料加熱気化器を不要とすることができる。よって
燃料噴霧ノズルにタールが詰まるといったことも解消で
きる。また直接接触により燃料を効率よく気化するの
で、高温空気の温度自体はタールが生じる温度よりも充
分に低く設定でき、空気加熱手段の必要電力等も低く抑
えることができる。また高温空気により多孔質燃焼板の
燃焼触媒を予備加熱するので、触媒層加熱器が不必要と
なり、また均一加熱ができ、触媒燃焼が安定して行え
る。また多孔質燃焼板の燃焼触媒を耐久温度以下に調整
し易く、また予熱時間も大幅に短縮できる。
According to the combustion apparatus of the present invention, the atomized vapor fuel is mixed with the hot air, so that the fuel is mixed with the normal temperature air. Since the fuel heating temperature by the heating vaporizer can be lowered, the generation of tar can be prevented and the fuel spray nozzle can be prevented from being clogged. Further, since the steam fuel is mixed with the high temperature air, reliquefaction of the steam fuel can be suppressed and tar can be prevented from adhering to the porous combustion plate. Further, since the combustion catalyst of the porous combustion plate is preheated by the high temperature air, the catalyst bed heater is not required, and uniform heating can be performed, so that the catalyst combustion can be stably performed. Further, it is easy to adjust the combustion catalyst of the porous combustion plate to a temperature not higher than the durability temperature, and the preheating time can be shortened significantly.
Further, according to the combustion device of the second aspect, since the air-fuel mixture that has been sufficiently mixed and vaporized in the vaporization chamber is used for combustion, the combustion can be further stabilized. Since the sprayed fuel can be vaporized and vaporized directly and sufficiently in contact with the hot air in the vaporization chamber, the conventional fuel heating vaporizer can be omitted. Therefore, it is possible to solve the problem that the fuel spray nozzle is clogged with tar. Further, since the fuel is efficiently vaporized by direct contact, the temperature itself of the high temperature air can be set sufficiently lower than the temperature at which tar is generated, and the power required by the air heating means and the like can be kept low. Further, since the combustion catalyst of the porous combustion plate is preheated by the high temperature air, the catalyst bed heater is not required, and uniform heating can be performed, so that the catalyst combustion can be stably performed. Further, it is easy to adjust the combustion catalyst of the porous combustion plate to a temperature not higher than the durability temperature, and the preheating time can be shortened significantly.

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

【図1】本発明装置の第1の実施例を示す燃焼装置の全
体の断面構成図である。
FIG. 1 is an overall sectional configuration diagram of a combustion device showing a first embodiment of the device of the present invention.

【図2】本発明装置の第2の実施例を示す燃焼装置の全
体の断面構成図である。
FIG. 2 is an overall cross-sectional configuration diagram of a combustion device showing a second embodiment of the device of the present invention.

【図3】図2の気化室を横からみた断面図である。3 is a cross-sectional view of the vaporization chamber of FIG. 2 seen from the side.

【図4】従来の燃焼装置の断面構成図である。FIG. 4 is a cross-sectional configuration diagram of a conventional combustion device.

【符号の説明】[Explanation of symbols]

51 送風器 52 燃料加熱気化器 53 燃料噴霧ノズル 54 多孔質燃焼板 61 空気加熱器 65 気化容器 66 気化室 51 Blower 52 Fuel heating vaporizer 53 Fuel spray nozzle 54 Porous combustion plate 61 Air heater 65 Vaporization vessel 66 Vaporization chamber

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 送風手段と、該送風手段からの空気を加
熱する加熱手段と、液体燃料の加熱気化手段と、該加熱
気化手段により蒸気化した燃料の噴霧供給手段とを有
し、前記噴霧供給手段により噴霧した蒸気化燃料に前記
加熱手段で得た高温空気を混合しながら、燃焼触媒を担
持した多孔質燃焼板に供給して燃焼させることを特徴と
する燃焼装置。
1. A spraying means, a heating means for heating air from the blowing means, a heating vaporizing means for a liquid fuel, and a spray supply means for spraying the fuel vaporized by the heating vaporizing means. A combustion apparatus, wherein the vaporized fuel sprayed by the supply means is mixed with the high-temperature air obtained by the heating means and is supplied to a porous combustion plate carrying a combustion catalyst for combustion.
【請求項2】 送風手段と、該送風手段からの空気を加
熱する加熱手段と、液体燃料の噴霧供給手段と、前記送
風手段から加熱手段を経て送り込まれる高温空気と前記
噴霧供給手段から吹き込まれた噴霧燃料とを直接的に接
触させて気化する気化室とを有し、気化室から送られて
くる混合気を燃焼触媒を担持した多孔質燃焼板で燃焼さ
せることを特徴とする燃焼装置。
2. Blower means, heating means for heating air from the blower means, spray supply means for liquid fuel, high temperature air sent from the blower means through the heating means, and blown from the spray supply means. And a vaporization chamber that directly vaporizes the atomized fuel to vaporize the mixture, and burns the air-fuel mixture sent from the vaporization chamber with a porous combustion plate carrying a combustion catalyst.
JP3876492A 1992-01-28 1992-01-28 Combustion equipment Pending JPH05203118A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3876492A JPH05203118A (en) 1992-01-28 1992-01-28 Combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3876492A JPH05203118A (en) 1992-01-28 1992-01-28 Combustion equipment

Publications (1)

Publication Number Publication Date
JPH05203118A true JPH05203118A (en) 1993-08-10

Family

ID=12534354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3876492A Pending JPH05203118A (en) 1992-01-28 1992-01-28 Combustion equipment

Country Status (1)

Country Link
JP (1) JPH05203118A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997021957A1 (en) * 1995-12-14 1997-06-19 Matsushita Electric Industrial Co., Ltd. Catalytic combustion apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997021957A1 (en) * 1995-12-14 1997-06-19 Matsushita Electric Industrial Co., Ltd. Catalytic combustion apparatus
US6431856B1 (en) 1995-12-14 2002-08-13 Matsushita Electric Industrial Co., Ltd. Catalytic combustion apparatus

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