JP2755358B2 - Heating device - Google Patents

Heating device

Info

Publication number
JP2755358B2
JP2755358B2 JP4196750A JP19675092A JP2755358B2 JP 2755358 B2 JP2755358 B2 JP 2755358B2 JP 4196750 A JP4196750 A JP 4196750A JP 19675092 A JP19675092 A JP 19675092A JP 2755358 B2 JP2755358 B2 JP 2755358B2
Authority
JP
Japan
Prior art keywords
combustion chamber
combustion
catalyst layer
catalyst
gas
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.)
Expired - Fee Related
Application number
JP4196750A
Other languages
Japanese (ja)
Other versions
JPH0642720A (en
Inventor
正人 保坂
次郎 鈴木
晃 前西
恭子 板谷
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 JP4196750A priority Critical patent/JP2755358B2/en
Priority to US08/062,608 priority patent/US5403184A/en
Priority to EP93108145A priority patent/EP0570933B1/en
Priority to DE69312798T priority patent/DE69312798T2/en
Publication of JPH0642720A publication Critical patent/JPH0642720A/en
Application granted granted Critical
Publication of JP2755358B2 publication Critical patent/JP2755358B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

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

【0001】[0001]

【産業上の利用分野】本発明はアイロン、スチーマ、調
理器、コーヒーメーカ等に用いられる、気体燃料または
液体燃料を燃焼し、その燃焼熱を熱源とする発熱装置に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating apparatus for burning gaseous or liquid fuel and using the heat of combustion as a heat source, which is used for irons, steamers, cookers, coffee makers and the like.

【0002】[0002]

【従来の技術】従来、燃焼熱を熱源とする発熱装置に
は、コードレスヘアカーラや懐炉等がある。これらのも
のは燃料にブタンガスやベンジンを使用し、燃料を気化
し空気と混合させた後、白金触媒を担持したフェルト状
の触媒に混合ガスを接触させて、触媒反応を行わせ、焼
熱を利用するものである。
2. Description of the Related Art Conventionally, there are cordless hair curlers, hand warmers and the like as heat generating devices using heat of combustion as a heat source. These use butane gas or benzene as fuel, evaporate the fuel and mix it with air, then contact the mixed gas with a felt-like catalyst carrying a platinum catalyst to cause a catalytic reaction and reduce the heat of combustion. To use.

【0003】[0003]

【発明が解決しようとする課題】上記の燃焼器は燃焼量
が少なく、触媒の温度が低い状態で燃焼が進行するもの
である。しかし、発熱量を増加すべく燃焼量を増加する
と、触媒層で反応すべき混合ガス量が増加するために、
混合ガスが触媒層ですべて反応できずに、未燃のまま排
出されるようになる。したがって燃焼量を増加するため
には、混合ガスが触媒層と接触する面積を増加しなけれ
ばならず、燃焼器が大きくなるという問題が生じる。
The above combustor has a small amount of combustion and the combustion proceeds in a state where the temperature of the catalyst is low. However, if the amount of combustion is increased to increase the calorific value, the amount of mixed gas to be reacted in the catalyst layer increases,
The mixed gas cannot be completely reacted in the catalyst layer, and is discharged unburned. Therefore, in order to increase the amount of combustion, the area where the mixed gas comes into contact with the catalyst layer must be increased, which causes a problem that the combustor becomes large.

【0004】本発明は上記従来技術の問題を解決するた
め、燃焼室が小さいコンパクトな発熱装置を提供するこ
とを目的とするものである。
An object of the present invention is to provide a compact heating device having a small combustion chamber in order to solve the above-mentioned problems of the prior art.

【0005】[0005]

【課題を解決するための手段】前記目的を達成するた
め、本発明の発熱装置は、燃料ガスと空気の混合部と、
前記混合部の下流に設けた内部に燃焼室を有する筺体を
少なくとも備えた発熱装置であって、混合ガスの流れ方
向に対して略平行に複数枚のフィンを前記燃焼室上面お
よび下面から燃焼室内に突出して交互に設け、前記フィ
ン先端と前記フィン先端に対向した前記燃焼室上面およ
び下面との間に隙間を設け、前記燃焼室内壁面およびフ
ィン壁面に触媒層を設けたことを特徴とする。
In order to achieve the above object, a heat generating apparatus according to the present invention comprises: a fuel gas / air mixing section;
A heating device provided with at least a housing having a combustion chamber inside provided downstream of the mixing section, wherein a plurality of fins are disposed substantially in parallel with a flow direction of a mixed gas from an upper surface and a lower surface of the combustion chamber. protrudes alternately provided, the gaps between the combustion chamber upper and lower surfaces fin tip and opposed to the fin tip provided, characterized in that a catalyst layer on the inner wall surface of the combustion chamber and the fin walls.

【0006】[0006]

【作用】前記本発明の構成によれば、混合ガスの流れ方
向に対して略平行に複数枚のフィンを前記燃焼室上面お
よび下面の交互に設け、前記フィン先端と前記燃焼室上
面および下面との間に隙間を設け、前記燃焼室内壁面お
よびフィン壁面に触媒層を設けたことにより、燃焼室が
小さいコンパクトな発熱装置とすることができる。すな
わち、燃焼室内にフィンを設け、フィン外壁面に触媒層
設けることにより、燃焼室の大きさを変えずに、触媒
面積を増加している。しかも、燃焼室内のフィンは燃焼
室の上面および下面に交互に設けてある。このようにす
ると燃焼室内に供給された予混合気は、燃焼室内に設け
られたフィンにより燃焼室内にほぼ均一に分散して、燃
焼室内を通過するようになる。このため、予混合気が効
率よく触媒表面に接触する。したがって触媒表面に接触
することなく燃焼室から排出する予混合気がほとんど存
在せず、燃焼効率が向上する。また、フィン壁面に設け
た触媒層は、加熱面である燃焼室内壁面と直接接触して
いないために、加熱面の加熱量の変動を受けにくく、触
媒表面の燃焼温度が高温に維持され、安定した燃焼を行
うことができる。しかも、高温で燃焼しているフィン先
端壁面の触媒層表面から燃焼室内壁面へ向けて燃焼熱が
輻射として供給されるために、燃焼室内壁面の温度低下
を防ぐことができる。従って、被加熱物の加熱量の変動
により生 じる燃焼室内壁面の触媒層の燃焼温度の変動を
防止することができる。
According to the configuration of the present invention, a plurality of fins are provided alternately on the upper and lower surfaces of the combustion chamber substantially in parallel to the flow direction of the mixed gas, and the fin tip and the upper and lower surfaces of the combustion chamber are provided. the gap between the provided, by providing the catalyst layer on the inner wall surface of the combustion chamber and the fin walls, can be a combustion chamber is small compact heating apparatus. That is, by providing the fins in the combustion chamber and providing the catalyst layer on the outer wall surfaces of the fins, the area of the catalyst is increased without changing the size of the combustion chamber. Moreover, the fins in the combustion chamber are provided alternately on the upper and lower surfaces of the combustion chamber. In this manner, the premixed gas supplied into the combustion chamber is substantially uniformly dispersed in the combustion chamber by the fins provided in the combustion chamber, and passes through the combustion chamber. For this reason, the premixed gas efficiently contacts the catalyst surface. Therefore, there is almost no premixed gas discharged from the combustion chamber without contacting the catalyst surface, and the combustion efficiency is improved. Also provided on the fin wall
The catalyst layer is in direct contact with the combustion chamber wall, which is the heating surface.
Is not easily affected by fluctuations in the amount of heating on the heating surface.
The combustion temperature on the medium surface is maintained at a high temperature, and stable combustion is performed.
I can. Moreover, the fin tip burning at high temperature
Combustion heat from the catalyst layer surface on the end wall toward the combustion chamber wall
As the radiation is supplied, the temperature of the combustion chamber wall decreases.
Can be prevented. Therefore, the fluctuation of the heating amount of the heated object
The variations in the combustion temperature of the catalyst layer of the arising combustion chamber wall
Can be prevented.

【0007】さらに、燃焼室内にフィンを設けることに
より触媒面積ばかりでなく、伝熱面積もが増加するため
に、触媒表面上における燃焼熱により被加熱物を加熱す
る熱交換効率が著しく向上する。したがって、燃焼室の
大きさを小さくできる。
Further, by providing the fins in the combustion chamber, not only the catalyst area but also the heat transfer area increases, so that the heat exchange efficiency of heating the object to be heated by the combustion heat on the catalyst surface is remarkably improved. Therefore, the size of the combustion chamber can be reduced.

【0008】[0008]

【実施例】以下実施例を用いて本発明をさらに具体的に
説明する。触媒燃焼とは、あらかじめ活性温度まで昇温
された触媒層表面に、燃料と空気の混合ガスが供給され
ると、触媒層表面近傍で触媒の働きにより、火炎燃焼に
比べて低温で混合ガスが燃焼し、発熱反応を生じる燃焼
現象のことである。したがって触媒燃焼において燃焼率
を高めるためには、いかに効率的に触媒表面に混合ガス
を供給するかということが重要になる。
The present invention will be described more specifically with reference to the following examples. Catalytic combustion means that when a mixed gas of fuel and air is supplied to the surface of a catalyst layer that has been heated to the activation temperature in advance, the catalyst works near the surface of the catalyst layer, and the mixed gas is cooled at a lower temperature than in flame combustion. A combustion phenomenon that burns and produces an exothermic reaction. Therefore, in order to increase the combustion rate in catalytic combustion, it is important how to efficiently supply the mixed gas to the catalyst surface.

【0009】このような触媒燃焼は触媒の表面で面燃焼
するために、触媒面の燃焼温度が燃焼特性に対して大き
な影響を及ぼす。一方、燃焼室の外壁面は熱板として被
加熱物へ熱量を供給するため、被加熱物への加熱量の変
動により触媒面の燃焼温度が変動することがある。本発
明は燃焼室の内壁面ばかりでなく、フィン外壁面に密着
した触媒面上での燃焼熱も、フィンを伝わり、燃焼室の
外壁面へ伝導し、被加熱物の加熱に寄与している。この
フィン外壁面に密着した触媒層は、加熱面と直接接触し
ていないために、加熱面の加熱量の変動を受けづらく、
触媒表面の燃焼温度が高温に維持され、安定した燃焼を
行うことができる。しかも、高温で燃焼している触媒層
表面から燃焼室内壁面へ燃焼熱が輻射として供給される
ために、被加熱物の加熱量の変動により生じる燃焼室内
壁面の触媒層の燃焼温度の変動を防止することができ
る。
In such catalytic combustion, surface combustion occurs on the surface of the catalyst, so that the combustion temperature on the catalyst surface has a great influence on the combustion characteristics. On the other hand, since the outer wall surface of the combustion chamber supplies heat to the object to be heated as a hot plate, the combustion temperature of the catalyst surface may fluctuate due to a change in the amount of heating to the object to be heated. In the present invention, not only the inner wall surface of the combustion chamber, but also the heat of combustion on the catalyst surface in close contact with the outer wall surface of the fins is transmitted through the fins, conducted to the outer wall surface of the combustion chamber, and contributes to heating of the object to be heated. . Since the catalyst layer in close contact with the outer wall surface of the fin is not in direct contact with the heating surface, it is difficult to receive a change in the heating amount of the heating surface,
The combustion temperature on the catalyst surface is maintained at a high temperature, and stable combustion can be performed. In addition, since combustion heat is supplied as radiation from the surface of the catalyst layer burning at high temperature to the combustion chamber wall surface, fluctuations in the combustion temperature of the catalyst layer on the wall surface of the combustion chamber caused by fluctuations in the heating amount of the object to be heated are prevented. can do.

【0010】以下、本発明の実施例を図面に基づいて説
明する。図1は本発明の一実施例の断面図である。図2
は図1におけるA−A方向矢視図である。図1において
1はプロパン、ブタン等の液化ガスボンベである。ボン
ベ1とノズル2の間にバルブ3が設けてあり、ボンベ1
から供給される燃料ガスの流量をコントロールできるよ
うにしている。ノズル2より噴出した燃料ガスは、ガス
流の誘引作用により回りの空気を吸引し、混合室4で均
一に混合し、燃焼室5に供給される。燃焼室5は金属製
の筺体で構成される発熱部6の内部に設けられている。
燃焼室5の内部には混合ガスの流れ方向に略平行に複数
枚のフィン7が設けられており、燃焼室5の大きさを変
えずに、燃焼室5内の表面積を増加している。
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a sectional view of one embodiment of the present invention. FIG.
FIG. 2 is a view taken in the direction of arrows AA in FIG. 1. In FIG. 1, reference numeral 1 denotes a liquefied gas cylinder such as propane or butane. A valve 3 is provided between the cylinder 1 and the nozzle 2.
To control the flow rate of fuel gas supplied from The fuel gas ejected from the nozzle 2 sucks the surrounding air by the attraction of the gas flow, is uniformly mixed in the mixing chamber 4, and is supplied to the combustion chamber 5. The combustion chamber 5 is provided inside a heat generating portion 6 formed of a metal housing.
A plurality of fins 7 are provided inside the combustion chamber 5 substantially parallel to the flow direction of the mixed gas, and the surface area of the combustion chamber 5 is increased without changing the size of the combustion chamber 5.

【0011】燃焼室5には触媒層8が燃焼室内壁面に設
けられている。触媒層8に担持される触媒は、白金族金
属およびニッケル、コバルト、鉄、マンガン、クロムな
どの金属酸化物が用いられるが、特に好ましいものは白
金、パラジウム、ロジウムなどの白金族金属である。触
媒層8の厚さが厚すぎると触媒層8での燃焼熱が発熱部
6へ供給されにくくなる。また、触媒層8の厚さが薄す
ぎると触媒層8における燃焼熱が発熱部6へ熱伝導しや
すくなり、触媒燃焼の際の燃焼温度の低下を引き起こ
し、燃焼不良が起こりやすくなる。そこで、触媒層8の
厚さとしては0.3mmから2.0mmが好ましい。乾
電池(図示せず)で細い白金線製点火ヒータ9が加熱さ
れ、さらに近接する触媒層8が高温化する。触媒層8が
活性温度まで加熱されたときに、バルブ3が開き、ノズ
ル2より燃料ガスが混合部4に供給される。このときの
動作は、燃焼室5内の温度をモニターして行ってもよい
し、点火ヒータ9に通電してから一定時間経過後にバル
ブ3を開いてもよい。燃料ガスの噴出力に誘引して吸引
された空気と燃料ガスが混合部4で混合し、混合ガスを
燃焼室5に供給する。燃焼室5では活性温度まで昇温さ
れた触媒層8表面に、燃料と空気の混合ガスが供給され
ると、触媒層8表面で混合ガスが燃焼を始める。燃焼室
5の入口近傍では、燃焼室内壁面の近傍に供給された混
合ガスのみが触媒層8近傍で燃焼するが、燃焼室5の中
心部付近の混合ガスは未燃のまま燃焼室5内を通過する
ことになる。したがって、燃焼室5を通過しているガス
は壁面近傍を燃焼ガスが流れ、その内側を混合ガスが流
れることになる。
In the combustion chamber 5, a catalyst layer 8 is provided on a wall surface of the combustion chamber. As the catalyst supported on the catalyst layer 8, a platinum group metal and a metal oxide such as nickel, cobalt, iron, manganese and chromium are used, and particularly preferred are platinum group metals such as platinum, palladium and rhodium. If the thickness of the catalyst layer 8 is too large, it becomes difficult for the heat of combustion in the catalyst layer 8 to be supplied to the heat generating portion 6. If the thickness of the catalyst layer 8 is too small, the heat of combustion in the catalyst layer 8 is likely to be conducted to the heat-generating portion 6, causing a decrease in the combustion temperature during the catalytic combustion and poor combustion. Therefore, the thickness of the catalyst layer 8 is preferably from 0.3 mm to 2.0 mm. The thin platinum wire ignition heater 9 is heated by a dry battery (not shown), and the temperature of the catalyst layer 8 closer to the heater becomes higher. When the catalyst layer 8 is heated to the activation temperature, the valve 3 opens, and fuel gas is supplied from the nozzle 2 to the mixing section 4. The operation at this time may be performed by monitoring the temperature in the combustion chamber 5, or the valve 3 may be opened after a certain period of time has elapsed after the ignition heater 9 is energized. The air and the fuel gas, which are attracted to the injection power of the fuel gas and mixed, are mixed in the mixing section 4, and the mixed gas is supplied to the combustion chamber 5. In the combustion chamber 5, when the mixed gas of fuel and air is supplied to the surface of the catalyst layer 8 heated to the activation temperature, the mixed gas starts burning on the surface of the catalyst layer 8. Near the inlet of the combustion chamber 5, only the mixed gas supplied near the wall of the combustion chamber burns near the catalyst layer 8, but the mixed gas near the center of the combustion chamber 5 passes through the combustion chamber 5 unburned. Will pass. Therefore, as for the gas passing through the combustion chamber 5, the combustion gas flows near the wall surface, and the mixed gas flows inside the combustion gas.

【0012】燃焼室5には混合ガスの流れ方向に対して
略平行にフィン7を設け、フィン7の外壁面に触媒層1
0を設けている。このため混合ガスは、フィン7の燃焼
面10aに衝突し、混合ガス中の未燃ガスの一部が燃焼
面10aで燃焼する。燃焼面10aと燃焼室5の入口近
傍で燃焼した燃焼ガスと、未燃の燃料ガスが混合し、フ
ィン7に密着した触媒層10と燃焼室5内壁面に密着し
た触媒層8の間を流れるようになる。このとき、高温の
燃焼ガスと未燃焼の燃料ガスが混合するため、燃料ガス
の温度を高める効果がある。この高温になった燃料ガス
が触媒層8と触媒層10との間の狭い隙間を流れていく
際に、未燃焼の燃焼ガスの実質的にすべてが燃焼する。
ここでフィン7は燃焼室5内に略平行に複数枚設けてあ
るために、予混合気は、フィン7により燃焼室5内にほ
ぼ均一に分散して、燃焼室5内を通過するようになる。
このため、予混合気が効率よく触媒表面に接触する。し
たがって触媒表面に接触することなく燃焼室5から排出
する予混合気がほとんど存在せず、燃焼効率が非常に向
上する。しかもフィン7は燃焼室5の片面だけではな
く、上面および下面に交互に設けてあるために、予混合
気の分散性がさらに向上し、予混合気が触媒面に非常に
効率的に接触するようになり、燃焼効率が非常に向上す
る。このため本実施例により、燃焼量を大きくしても燃
焼室5が小さいコンパクトな発熱装置にすることができ
る。
Fins 7 are provided in the combustion chamber 5 substantially in parallel with the flow direction of the mixed gas.
0 is provided . Therefore, the mixed gas collides with the combustion surface 10a of the fin 7, and a part of the unburned gas in the mixed gas burns on the combustion surface 10a. The combustion gas burned in the vicinity of the combustion surface 10a and the inlet of the combustion chamber 5 and the unburned fuel gas are mixed and flow between the catalyst layer 10 adhered to the fin 7 and the catalyst layer 8 adhered to the inner wall surface of the combustion chamber 5. Become like At this time, since the high-temperature combustion gas and the unburned fuel gas are mixed, there is an effect of increasing the temperature of the fuel gas. As the heated fuel gas flows through the narrow gap between the catalyst layers 8 and 10, substantially all of the unburned combustion gas is burned.
Here, since a plurality of fins 7 are provided substantially in parallel in the combustion chamber 5, the premixed gas is substantially uniformly dispersed in the combustion chamber 5 by the fins 7 and passes through the combustion chamber 5. Become.
For this reason, the premixed gas efficiently contacts the catalyst surface. Therefore, there is almost no premixed gas discharged from the combustion chamber 5 without contacting the catalyst surface, and the combustion efficiency is greatly improved. In addition, since the fins 7 are alternately provided not only on one side of the combustion chamber 5 but also on the upper surface and the lower surface, the dispersibility of the premixed gas is further improved, and the premixed gas contacts the catalyst surface very efficiently. And the combustion efficiency is greatly improved. For this reason, according to the present embodiment, a compact heat generating device in which the combustion chamber 5 is small even when the amount of combustion is increased can be provided.

【0013】この時、触媒層8と触媒層10の隙間は広
すぎると効果がなくり、ファイバー状の多孔質材料をア
ルミ製の燃焼室に接着して実験した結果、触媒層8と触
媒層10との隙間を4mm以下にすると効果が大きいこ
とが確認できた。
At this time, if the gap between the catalyst layer 8 and the catalyst layer 10 is too wide, the effect is lost. The experiment was conducted by bonding a fibrous porous material to an aluminum combustion chamber. It was confirmed that the effect was great when the gap with 10 was 4 mm or less.

【0014】触媒表面で発生した燃焼ガスは、触媒層8
と触媒層10との間の狭い隙間を流れるために、燃焼ガ
スの流速が速くなり、燃焼ガス側の熱伝達率が大きくな
り、発熱部6での熱交換効率が向上する。
The combustion gas generated on the catalyst surface is transferred to the catalyst layer 8.
Since the gas flows through the narrow gap between the fuel gas and the catalyst layer 10, the flow velocity of the combustion gas increases, the heat transfer coefficient on the combustion gas side increases, and the heat exchange efficiency in the heat generating portion 6 improves.

【0015】触媒燃焼は触媒の表面で面燃焼するため
に、触媒面の燃焼温度が燃焼特性に対して大きな影響を
及ぼす。一方、燃焼室5の外壁面は発熱部6とで被加熱
物へ熱量を供給するため、被加熱物への加熱量の変動に
より触媒面8の燃焼温度が変動することがある。本実施
例は燃焼室5の内壁面ばかりでなく、フィン7外壁面に
設けた触媒層10表面上での燃焼熱も、フィン7を伝わ
り、燃焼室5の外壁面にある発熱部6へ伝導し、被加熱
物の加熱に寄与している。このフィン7外壁面に密着し
た触媒層10は、発熱部6と直接接触していないため
に、発熱部6の加熱量の変動の影響を受けづらく、触媒
層表面の燃焼温度が高温に維持され、安定した燃焼を行
うことができる。しかも、高温で燃焼している触媒層1
0表面から燃焼室内壁面の触媒層8へ燃焼熱が輻射とし
て供給されるために、被加熱物の加熱量の変動により生
じる燃焼室内壁面の触媒層8の燃焼温度の変動を防止す
ることができる。
[0015] Since catalytic combustion involves surface combustion on the surface of the catalyst, the combustion temperature on the catalyst surface has a significant effect on combustion characteristics. On the other hand, since the outer wall surface of the combustion chamber 5 supplies heat to the object to be heated by the heat generating portion 6, the combustion temperature of the catalyst surface 8 may fluctuate due to a change in the amount of heating to the object to be heated. The present embodiment is applied not only to the inner wall surface of the combustion chamber 5 but also to the outer wall surface of the fin 7.
The heat of combustion on the surface of the catalyst layer 10 provided also propagates through the fins 7 and is conducted to the heat generating portion 6 on the outer wall surface of the combustion chamber 5 to contribute to heating of the object to be heated. Since the catalyst layer 10 in close contact with the outer wall surface of the fin 7 is not in direct contact with the heat generating portion 6, the catalyst layer 10 is hardly affected by a change in the heating amount of the heat generating portion 6, and the combustion temperature on the catalyst layer surface is maintained at a high temperature. , And stable combustion can be performed. Moreover, the catalyst layer 1 burning at high temperature
Since combustion heat is supplied as radiation from the surface 0 to the catalyst layer 8 on the wall surface of the combustion chamber, it is possible to prevent fluctuations in the combustion temperature of the catalyst layer 8 on the wall surface of the combustion chamber caused by fluctuations in the amount of heating of the object to be heated. .

【0016】燃焼室5内でクリーンに燃焼した燃焼ガス
は、排気口11より排出される。また、発熱部6には温
度検出部12が設けられている。温度検出部12は、発
熱部6の温度をモニタし、その信号をバルブ3に送り、
バルブ3の開度を調節することにより、燃焼量を調節す
る働きを有している。このため、発熱部6の表面温度は
一定に保たれ、被加熱物を最適な温度で加熱することが
できる。
The combustion gas cleanly burned in the combustion chamber 5 is discharged from an exhaust port 11. In addition, the heat generating unit 6 is provided with a temperature detecting unit 12. The temperature detection unit 12 monitors the temperature of the heating unit 6 and sends a signal to the valve 3,
Adjusting the opening of the valve 3 has the function of adjusting the amount of combustion. For this reason, the surface temperature of the heat generating portion 6 is kept constant, and the object to be heated can be heated at an optimum temperature.

【0017】図2に示すように、燃焼室5内のフィン先
端と前記燃焼室内壁面との間に隙間を設けることによ
り、触媒層10の上面10bと燃焼室5の内壁面に設け
た触媒層8aとの間に隙間を設けてある。このようにす
ることにより、フィン7先端の触媒層10bから燃焼室
5の内壁面の触媒層8へ燃焼熱が輻射熱として供給され
る。しかもフィン7は燃焼室5の上面および下面に交互
に設けられているために、フィンに設けた触媒層10か
らの輻射熱は燃焼室5の内壁面実質的なすべてに供給さ
れるようになる。このために、被加熱物の加熱量の変動
により生じる燃焼室内壁面の触媒層8の温度の変動を防
止することができ、触媒層表面での燃焼温度の低下を防
ぎ、触媒の活性を維持することができる。
As shown in FIG. 2, by providing a gap between the fin tip in the combustion chamber 5 and the wall surface of the combustion chamber, the upper surface 10b of the catalyst layer 10 and the catalyst layer provided on the inner wall surface of the combustion chamber 5 are provided. 8a. By doing so, the combustion heat is supplied as radiant heat from the catalyst layer 10b at the tip of the fin 7 to the catalyst layer 8 on the inner wall surface of the combustion chamber 5. Moreover, since the fins 7 are alternately provided on the upper surface and the lower surface of the combustion chamber 5, the radiant heat from the catalyst layer 10 provided on the fins is supplied to substantially all the inner wall surfaces of the combustion chamber 5. For this reason, it is possible to prevent a change in the temperature of the catalyst layer 8 on the wall surface of the combustion chamber caused by a change in the heating amount of the object to be heated, prevent a decrease in the combustion temperature on the surface of the catalyst layer, and maintain the activity of the catalyst. be able to.

【0018】したがって、加熱量の変動に対しても燃焼
特性を良好に維持することができ、燃焼室が小さいコン
パクトな発熱装置にすることができる。
Therefore, good combustion characteristics can be maintained even with fluctuations in the amount of heating, and a compact heat generating apparatus with a small combustion chamber can be provided.

【0019】[0019]

【発明の効果】以上のように本発明は、燃料ガスと空気
の混合部と、混合部の下流に設けた内部に燃焼室を有す
る筺体とから構成され、混合ガスの流れ方向に対して平
行に複数のフィンを燃焼室上面および下面の交互に設
け、フィン先端と燃焼室上面あるいは下面との間に隙間
を設け、燃焼室内壁面およびフィン壁面に触媒層を設け
たことにより、効率的に触媒層表面に燃料ガスを接触さ
せ、かつ発熱部における加熱量の変動により生じる触媒
温度の変動を防ぎ、コンパクトな発熱装置にすることが
できる。
As described above, the present invention comprises a mixing section for fuel gas and air, and a housing provided downstream of the mixing section and having a combustion chamber therein, and is parallel to the flow direction of the mixed gas. A plurality of fins are alternately provided on the upper and lower surfaces of the combustion chamber, a gap is provided between the fin tip and the upper or lower surface of the combustion chamber, and a catalyst layer is provided on the wall surface of the combustion chamber and the fin wall surface, so that a catalyst can be efficiently provided. The fuel gas is brought into contact with the surface of the layer, and a change in the catalyst temperature caused by a change in the amount of heating in the heat generating portion is prevented.

【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発熱装置の水平断面
図である。
FIG. 1 is a horizontal sectional view of a heat generating device according to an embodiment of the present invention.

【図2】本発明の同装置の垂直断面図(図1のA−A方
向矢視図)である。
FIG. 2 is a vertical cross-sectional view of the same device of the present invention (a view in the direction of arrows AA in FIG. 1).

【符号の説明】[Explanation of symbols]

2 ノズル 4 混合部 5 燃焼室 6 発熱部 7 フィン 8、10 触媒層 2 Nozzle 4 Mixing part 5 Combustion chamber 6 Heating part 7 Fin 8, 10 Catalyst layer

───────────────────────────────────────────────────── フロントページの続き (72)発明者 板谷 恭子 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 平5−231623(JP,A) 特開 昭58−49809(JP,A) 実開 昭57−36415(JP,U) 特公 昭43−25876(JP,B1) (58)調査した分野(Int.Cl.6,DB名) F23D 14/00 - 14/18 F23D 14/26 - 14/84 F23C 3/00 F23C 11/00 306 F23D 11/40────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kyoko Itaya 1006 Kazuma Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-5-231623 (JP, A) JP-A-58- 49809 (JP, A) Japanese Utility Model Showa 57-36415 (JP, U) Japanese Patent Publication No. 43-25876 (JP, B1) (58) Fields investigated (Int. Cl. 6 , DB name) F23D 14/00-14 / 18 F23D 14/26-14/84 F23C 3/00 F23C 11/00 306 F23D 11/40

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 燃料ガスと空気の混合部と、前記混合部
の下流に設けた内部に燃焼室を有する筺体を少なくとも
備えた発熱装置であって、混合ガスの流れ方向に対して
略平行に複数枚のフィンを前記燃焼室上面および下面
ら燃焼室内に突出して交互に設け、前記フィン先端と前
記フィン先端に対向した前記燃焼室上面および下面との
間に隙間を設け、前記燃焼室内壁面およびフィン壁面に
触媒層を設けたことを特徴とする発熱装置。
1. A heat generating apparatus comprising at least a housing having a mixing section of fuel gas and air and a combustion chamber provided downstream of the mixing section, and substantially parallel to a flow direction of the mixed gas. Whether a plurality of fins are on the upper and lower surfaces of the combustion chamber
And alternately protruding into the combustion chamber, a gap is provided between the fin tip and the upper and lower surfaces of the combustion chamber opposed to the fin tip , and a catalyst layer is provided on the combustion chamber wall and the fin wall. Heating device.
JP4196750A 1992-05-20 1992-07-23 Heating device Expired - Fee Related JP2755358B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP4196750A JP2755358B2 (en) 1992-07-23 1992-07-23 Heating device
US08/062,608 US5403184A (en) 1992-05-20 1993-05-18 Exothermic apparatus
EP93108145A EP0570933B1 (en) 1992-05-20 1993-05-19 Exothermic apparatus
DE69312798T DE69312798T2 (en) 1992-05-20 1993-05-19 Exothermic device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4196750A JP2755358B2 (en) 1992-07-23 1992-07-23 Heating device

Publications (2)

Publication Number Publication Date
JPH0642720A JPH0642720A (en) 1994-02-18
JP2755358B2 true JP2755358B2 (en) 1998-05-20

Family

ID=16362992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4196750A Expired - Fee Related JP2755358B2 (en) 1992-05-20 1992-07-23 Heating device

Country Status (1)

Country Link
JP (1) JP2755358B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69816326T2 (en) 1997-10-16 2004-04-22 Toyota Jidosha K.K., Toyota CATALYTIC COMBUSTION HEATER
JP3863979B2 (en) * 1997-10-20 2006-12-27 株式会社日本自動車部品総合研究所 Catalytic combustion heating device
EP1643094B1 (en) * 2004-10-01 2009-06-17 J. Eberspächer GmbH & Co. KG Exhaust system for an internal combustion engine and corresponding operating method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5736415U (en) * 1980-08-11 1982-02-26
JPS5849809A (en) * 1981-09-18 1983-03-24 Matsushita Electric Ind Co Ltd Catalytic combustor
JPH05231623A (en) * 1992-02-19 1993-09-07 Babcock Hitachi Kk Catalyst combustion device

Also Published As

Publication number Publication date
JPH0642720A (en) 1994-02-18

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