JP2812062B2 - Heating device - Google Patents
Heating deviceInfo
- Publication number
- JP2812062B2 JP2812062B2 JP4127069A JP12706992A JP2812062B2 JP 2812062 B2 JP2812062 B2 JP 2812062B2 JP 4127069 A JP4127069 A JP 4127069A JP 12706992 A JP12706992 A JP 12706992A JP 2812062 B2 JP2812062 B2 JP 2812062B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- combustion chamber
- catalyst layer
- catalyst
- wall surface
- 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
Links
Landscapes
- Combustion Of Fluid Fuel (AREA)
- Gas Burners (AREA)
- Spray-Type Burners (AREA)
Description
【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 heat generating apparatus used for irons, steamers, cookers, coffee makers, etc., which burns gaseous or liquid fuel and uses the heat of combustion as a heat source.
【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、燃
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 fuels 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課題が生じる。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, causing a problem that the size of the combustor increases.
【0004】本発明は上記従来技術の課題を解決するこ
とができ、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 solve the above-mentioned problems of the prior art and to provide a compact heat generating device having a small combustion chamber.
【0005】[0005]
【課題を解決するための手段】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、燃焼室内に混合気の流れ方向
に略平行にフィンを設け、燃焼室内壁面およびフィンの
外壁面に触媒層を密着させたことからなるものである。According to the present invention, there is provided a fuel gas and air mixing section, and a housing provided downstream of the mixing section and having a combustion chamber therein. The fins are provided substantially in parallel, and the catalyst layer is brought into close contact with the wall surfaces of the combustion chamber and the outer wall surfaces of the fins.
【0006】また、燃焼室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たことからなるものである。Further, a gap is provided between a fin tip in the combustion chamber and a wall surface of the combustion chamber.
【0007】[0007]
【作用】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、如何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。本発明はこのこと
を鑑がみて行われたものである。[Function] Catalytic combustion means that when a mixed gas of fuel and air is supplied to the surface of the catalyst layer which has been heated to the activation temperature in advance, the catalyst works near the surface of the catalyst layer and the temperature is lower than that of flame combustion. This is a combustion phenomenon in which the mixed gas burns to generate 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. The present invention has been made in view of the above.
【0008】本発明では燃焼室内にフィンを設け、フィ
ン外壁面に触媒層を密着させることにより、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、燃焼室の大きさを非常に小さくで
きる。In the present invention, the fin is provided in the combustion chamber, and the catalyst layer is brought into close contact with the outer wall surface of the fin, thereby increasing the catalyst area without changing the size of the combustion chamber. Moreover, 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 for 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 made very small.
【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】[0010]
【実施例】以下、本願発明の実施例を添付図面に基づい
て説明する。Embodiments of the present invention will be described below with reference to the accompanying drawings.
【0011】図1は本願発明の一実施例の断面図であ
る。図2は図1におけるAA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
は金属性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
行にフィン7が設けられており、伝熱面積を増加するこ
とにより、触媒表面上における燃焼熱の熱交換効率を向
上することができる。FIG. 1 is a sectional view of an embodiment of the present invention. FIG. 2 is a view in the direction of arrows AA in FIG. 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,
The flow rate of the fuel gas supplied from the cylinder 1 can be controlled. 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. Combustion chamber 5
Is provided inside the heat generating section 6 which is formed of a metal housing. Fins 7 are provided in the combustion chamber 5 in a direction substantially parallel to the flow direction of the mixed gas. By increasing the heat transfer area, the heat exchange efficiency of combustion heat on the catalyst surface can be improved.
【0012】燃焼室5には触媒層8が燃焼室内壁面に密
着して設けられている。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より燃焼ガスが混合部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 in close contact with the wall surface of the combustion chamber. A thin platinum wire ignition heater 9 is heated by a dry battery (not shown), and a catalyst layer 8 which is closer to the platinum wire is heated.
Temperature rises. When the catalyst layer 8 is heated to the activation temperature, the valve 3 is opened and the combustion gas is
Supplied to 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.
【0013】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外壁面に触媒層10
を密着させている。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
の燃焼ガスと未燃の燃料ガスが混合しするため、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、未燃の燃焼ガスのすべてが燃焼する。触媒層8
と触媒層10の隙間は広すぎると効果がなくなる。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された。Fins 7 are provided in the combustion chamber 5 substantially parallel to the flow direction of the mixed gas, and a catalyst layer 10
Is in close contact. 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 near the combustion surface 10a and the inlet of the combustion chamber 5 and the unburned fuel gas are mixed,
The fuel flows between the catalyst layer 10 closely attached to the fins 7 and the catalyst layer 8 closely attached to the inner wall surface of the combustion chamber 5. 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. When the high-temperature fuel gas flows through the narrow gap between the catalyst layer 8 and the catalyst layer 10, all of the unburned combustion gas is burned. Catalyst layer 8
If the gap between the catalyst layer and the catalyst layer 10 is too wide, the effect is lost. As a result of an experiment in which a fibrous porous material was bonded to a combustion chamber made of aluminum, it was confirmed that the effect was large when the gap between the catalyst layers 8 and 10 was 4 mm or less.
【0014】しかも燃焼ガスが触媒層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
の熱交換効率を向上する。Further, since the combustion gas flows through the narrow gap between the catalyst layer 8 and the catalyst layer 10, the flow velocity of the combustion gas increases, the heat transfer coefficient on the combustion gas side increases, and Improve exchange efficiency.
【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8の燃焼温度が変動することがある。本発明
は燃焼室5の内壁面ばかりでなく、フィン7外壁面に密
着した触媒層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 as the heat generating portion 6, the combustion temperature of the catalyst surface 8 may fluctuate due to a change in the amount of heat applied to the object to be heated. According to the present invention, not only the inner wall surface of the combustion chamber 5 but also the heat of combustion on the surface of the catalyst layer 10 adhered to the outer wall surface of the fin 7 is transmitted through the fin 7 and transmitted to the heat generating portion 6 on the outer wall surface of the combustion chamber 5. Contributes to the 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3は本願発明の他実施例の燃焼室5の断
面図(図1のAA方向矢視図に対応)である。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
壁面に密着した触媒層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、いままで触媒燃焼に寄与し
ていなかったフィン7先端の触媒層10b表面上でも触
媒燃焼を行うようになり、燃焼に有効な触媒面積を増加
することができ、燃焼率をさらに向上することができ
る。加えてフィン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た
めに、されて触媒層13の下面13bから輻射熱の供給
を受け、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、触媒の活性を維持することができる。FIG. 3 is a sectional view (corresponding to a view taken in the direction of arrows AA in FIG. 1) of a combustion chamber 5 according to another embodiment of the present invention. Combustion chamber 5
By providing a gap between the tip of the inner fin and the wall surface of the combustion chamber, a gap is provided between the upper surface 10b of the catalyst layer 10 and the catalyst layer 8a closely attached to the inner wall surface of the combustion chamber 5.
By doing so, catalytic combustion can be performed even on the surface of the catalyst layer 10b at the tip of the fin 7, which has not contributed to catalytic combustion so far, and the effective catalytic area for combustion can be increased, and the combustion rate can be increased. Can be further improved. In addition, since the combustion heat is supplied as radiant heat from the catalyst layer 10 b at the tip of the fin 7 to the catalyst layer 8 on the inner wall surface of the combustion chamber 5, the radiant heat is supplied from the lower surface 13 b of the catalyst layer 13, The fluctuation of the combustion temperature of the catalyst layer 8 on the wall surface of the combustion chamber caused by the fluctuation of the heating amount can be prevented, and the activity of the catalyst can be maintained.
【0018】また、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、燃焼室5の
流路断面積が広くなる。このために燃焼室5内の圧力損
失が小さくなり、燃料ガスの噴出力により誘引される空
気の吸引がしやすくなり、燃焼用空気の供給が安定して
行えるという効果もある。Further, by providing a gap between the tip of the fin in the combustion chamber 5 and the wall surface of the combustion chamber, the flow passage cross-sectional area of the combustion chamber 5 is increased. For this reason, the pressure loss in the combustion chamber 5 is reduced, and the air induced by the injection power of the fuel gas is easily sucked, so that the combustion air can be supplied stably.
【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、燃焼室内に混合気の流れ方向に
略平行にフィンを設け、燃焼室内壁面およびフィンの外
壁面に触媒層を密着させたことにより、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 inside the mixing section and having a combustion chamber inside the mixing section. The fins are provided substantially in parallel, and the catalyst layer is brought into close contact with the inner wall surface of the combustion chamber and the outer wall surface of the fins, so that the fuel gas can be efficiently brought into contact with the surface of the catalyst layer. Fluctuations can be prevented and a compact heating device can be provided.
【図1】本願発明の一実施例における発熱装置の水平断
面図FIG. 1 is a horizontal sectional view of a heating device according to an embodiment of the present invention.
【図2】本願発明の同装置の垂直断面図(図1のAA方
向矢視図)FIG. 2 is a vertical cross-sectional view of the same device according to the present invention (as viewed in the direction of arrows AA in FIG. 1).
【図3】本願発明の他実施例における発熱装置の燃焼室
の垂直断面図FIG. 3 is a vertical sectional view of a combustion chamber of a heating device according to another embodiment of the present invention.
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 昭61−184319(JP,A) 特開 昭61−72912(JP,A) 特開 平3−125807(JP,A) 特公 昭48−38728(JP,B1) (58)調査した分野(Int.Cl.6,DB名) F23D 11/40,14/04 F23C 3/00,11/00────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kyoko Itaya 1006 Kazuma Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-61-184319 (JP, A) JP-A-61- 72912 (JP, A) JP-A-3-125807 (JP, A) JP-B-48-38728 (JP, B1) (58) Fields investigated (Int. Cl. 6 , DB name) F23D 11/40, 14 / 04 F23C 3 / 00,11 / 00
Claims (1)
部の下流に設けた内部に燃焼室を有する筐体を少なくと
も備えた発熱装置であって、前記混合ガスの流れ方向に
対して略平行にフィンを前記燃焼室の壁面より前記燃焼
室の内部に向けて突出して設け、前記フィン先端と前記
燃焼室内壁面との間に隙間を設け、さらに前記燃焼室の
内壁面および前記フィンの外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 mixing section of fuel gas and air, and a housing provided with a combustion chamber inside provided downstream of the mixing section, wherein provided with fins substantially parallel to protrude toward the inside of the combustion chamber than the wall surface of the combustion chamber, the said fin tip
A heat generating device , wherein a gap is provided between a wall of the combustion chamber and a catalyst layer is provided on an inner wall of the combustion chamber and an outer wall of the fin.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4127069A JP2812062B2 (en) | 1992-05-20 | 1992-05-20 | Heating device |
US08/062,608 US5403184A (en) | 1992-05-20 | 1993-05-18 | Exothermic apparatus |
DE69312798T DE69312798T2 (en) | 1992-05-20 | 1993-05-19 | Exothermic device |
EP93108145A EP0570933B1 (en) | 1992-05-20 | 1993-05-19 | Exothermic apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4127069A JP2812062B2 (en) | 1992-05-20 | 1992-05-20 | Heating device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05322125A JPH05322125A (en) | 1993-12-07 |
JP2812062B2 true JP2812062B2 (en) | 1998-10-15 |
Family
ID=14950815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4127069A Expired - Fee Related JP2812062B2 (en) | 1992-05-20 | 1992-05-20 | Heating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2812062B2 (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4838728A (en) * | 1971-09-17 | 1973-06-07 | ||
JPS6172912A (en) * | 1984-09-14 | 1986-04-15 | Matsushita Electric Ind Co Ltd | Catalytic combustion device |
JPS61184319A (en) * | 1985-02-12 | 1986-08-18 | Nippon Shokubai Kagaku Kogyo Co Ltd | Method of generating hot blast by catalytic combustion |
JPH03125807A (en) * | 1989-10-06 | 1991-05-29 | Babcock Hitachi Kk | Catalytic burner |
-
1992
- 1992-05-20 JP JP4127069A patent/JP2812062B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05322125A (en) | 1993-12-07 |
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