JPS5864412A - Catalytic combustion equipment - Google Patents

Catalytic combustion equipment

Info

Publication number
JPS5864412A
JPS5864412A JP16325881A JP16325881A JPS5864412A JP S5864412 A JPS5864412 A JP S5864412A JP 16325881 A JP16325881 A JP 16325881A JP 16325881 A JP16325881 A JP 16325881A JP S5864412 A JPS5864412 A JP S5864412A
Authority
JP
Japan
Prior art keywords
catalytic combustion
layer
temperature
combustion layer
combustion
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
JP16325881A
Other languages
Japanese (ja)
Inventor
Masaaki Yonemura
米村 正明
Ikuo Matsumoto
松本 郁夫
Ryoji Shimada
良治 島田
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 JP16325881A priority Critical patent/JPS5864412A/en
Publication of JPS5864412A publication Critical patent/JPS5864412A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C13/00Apparatus in which combustion takes place in the presence of catalytic material

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gas Burners (AREA)
  • Spray-Type Burners (AREA)

Abstract

PURPOSE:To enable to detect the completion of preheating, slip, abnormal heating and the like of a catalytic combustion layer by measuring the temperature change of the catalytic combustion layer and consequently improve the safety and reliability of the equipment by a structure wherein a temperature detecting element is provided on the outer wall of a combustion tube at the location, to which the catalytic combustion layer is fixed. CONSTITUTION:In the titled equipment, liquid fuel supplied from a feed oil 29 and combustion air charged by means of a fan 8 are pre-mixed in an evaporation premixing chamber 16 and then sent through a resistance plate 15 and a straightening element 18 into a space 21 to be ignited and burnt there. Consequently, the catalytic combustion layer 20 is preheated with a small flame produced within the space 21. In this case, when the temperature of said layer 20 reaches the predetermined temperature, a controlling circuit (not shown) is assumed to be changed-over by means of the temperature detecting element 25 provided on the outer wall of the combustion tube 13. Concretely, air is increased to the flow amount, at which the oxidation reaction in the combustion layer 20 is allowed, by controlling a damper and, after the increase of the air, controlled so as to be increased to the steady flow amount with a suitable time lag after the extinction of lifted flame.

Description

【発明の詳細な説明】 本発明はガス燃料または液体燃料を気化させたガス状燃
料と空気を予混合させた予混合ガスを触媒燃焼層に供給
し、触媒酸化反応をおこさせる装置であって、装置起動
時に触媒酸化反応を維持するのに充分な温度に達したこ
とを検知するとともに、定常の触媒燃焼下においては触
媒燃焼層の温度をモニタしており、吹き飛びを生じた場
合にはその異常を検知する検知手段に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention is an apparatus for supplying a premixed gas prepared by premixing gaseous fuel or gaseous fuel obtained by vaporizing liquid fuel and air to a catalytic combustion layer to cause a catalytic oxidation reaction. , it detects when the device starts up that the temperature has reached sufficient to maintain the catalytic oxidation reaction, and also monitors the temperature of the catalytic combustion layer during steady catalytic combustion, and if blow-out occurs, the temperature is The present invention relates to a detection means for detecting an abnormality.

従来、タービンやボイラに応、剛化を図っている触媒燃
焼装置では、定常時に燃料を供給するメインノズルの他
にパイロットバーナを設け、このパイロットバーナを一
定時間燃焼させて触媒燃焼層を予熱するものであり、予
熱不足により鍮媒燃暁層で燃料が完全に酸化されず、−
着化炭素や未燃成分を排出する場合があった。さらに、
触媒活性の劣化や供給空気量や燃料供給量が異常に変化
した場合など、吹飛びや過熱などの異常状態を生じてい
た。本発明はこれらの点に鑑み、触媒燃焼層装着部分の
燃焼筒外壁に温度検知素子を取付け、触媒燃焼層の温度
を間接的に測定することで予熱完了や吹飛び、異常過熱
などを検知するものである。
Conventionally, catalytic combustion equipment has been designed to be more rigid in accordance with turbines and boilers.In addition to the main nozzle that supplies fuel during steady state, a pilot burner is installed, and this pilot burner is burned for a certain period of time to preheat the catalytic combustion layer. Due to insufficient preheating, the fuel is not completely oxidized in the brass-fuel combustion layer, and -
In some cases, carbonized carbon and unburned components were emitted. moreover,
Abnormal conditions such as blow-off and overheating have occurred due to deterioration of catalyst activity or abnormal changes in the amount of supplied air or fuel. In view of these points, the present invention installs a temperature detection element on the outer wall of the combustion cylinder where the catalytic combustion layer is installed, and indirectly measures the temperature of the catalytic combustion layer to detect completion of preheating, blow-out, abnormal overheating, etc. It is something.

以下に、液体燃料の気化予混合ブロックとしてロータリ
気化方式を採用した触媒燃焼層装置を一実施例として第
1図に示し、その構成を述べる。
A catalytic combustion layer device employing a rotary vaporization method as a vaporization premixing block for liquid fuel is shown as an example in FIG. 1 below, and its configuration will be described.

1は有底円筒状のファンケースで、底部には吸気導入口
2が開口しており、外方に金具3によりファンケース1
底部にモータ4を固定し、モータ4のシャフト5はファ
ンケース1の中心線に沿って吸気導入口2からファンケ
ース1内に挿入されている。モータ4は吸気口6を有す
るモータケース7によって覆われている。シャフト5に
はファン8が、またファンケース1には案内羽根9が固
定され、それぞれ交互に多段に設けられている。
1 is a cylindrical fan case with a bottom, an air intake inlet 2 is opened at the bottom, and a metal fitting 3 connects the fan case 1 to the outside.
A motor 4 is fixed to the bottom, and a shaft 5 of the motor 4 is inserted into the fan case 1 from an air intake inlet 2 along the center line of the fan case 1. The motor 4 is covered by a motor case 7 having an air intake 6 . A fan 8 is fixed to the shaft 5, and guide blades 9 are fixed to the fan case 1, and these are provided alternately in multiple stages.

一方、ファンケース1の他端には中央に送気口10を有
する固定板11が嵌合され、ファンケース1外方に向は
バンキング12を介して燃焼筒13が装着されている。
On the other hand, a fixing plate 11 having an air supply port 10 in the center is fitted to the other end of the fan case 1, and a combustion tube 13 is attached to the outside of the fan case 1 via a banking 12.

固定板11近傍の燃焼筒13側壁にはシーズヒータ14
が埋設され、金網あるいはパンチングメタルの抵抗板1
5と固定板11に囲まれる空間を気化予混合室16とし
ている。さらに燃焼筒13内の抵抗板15にはスペーサ
17を介して整流作用を行なう、ハニカム成形体である
整流素子18、保持金具19、触媒燃焼層2゜が順次装
着されており、これらに囲まれる空間21には燃焼筒1
3、保持金具19を貫通して点火プラグ22が空間21
内に臨むよ′う固定されている。
A sheathed heater 14 is installed on the side wall of the combustion tube 13 near the fixed plate 11.
is buried, and resistance plate 1 made of wire mesh or punched metal
5 and the fixed plate 11 is defined as a vaporization premixing chamber 16. Furthermore, a rectifying element 18 which is a honeycomb molded body that performs a rectifying action through a spacer 17, a holding fitting 19, and a catalytic combustion layer 2° are attached to the resistance plate 15 in the combustion tube 13 in this order, and is surrounded by these elements. In the space 21 there is a combustion tube 1
3. The spark plug 22 passes through the holding fitting 19 and enters the space 21
It is fixed so that it faces inside.

触媒燃焼層2oは白金族金嘱やi異金属酸化物等を担持
させたアルミナ、コーディエライト、ムラしている。2
3は押え金具で触媒燃焼層2oを・燃焼筒13内に用定
している。燃焼筒13の先端開口部は熱交換器24に接
続されており、燃焼筒13の触媒燃焼層2o挿入部外壁
には本発明に係る〆都度検知素子25を取付けである。
The catalytic combustion layer 2o is made of alumina, cordierite, and other materials supporting platinum group metals, oxides of different metals, and the like. 2
Reference numeral 3 denotes a presser fitting that holds the catalytic combustion layer 2o inside the combustion tube 13. The opening at the tip of the combustion tube 13 is connected to a heat exchanger 24, and a detection element 25 according to the present invention is attached to the outer wall of the insertion portion of the catalytic combustion layer 2o of the combustion tube 13.

一方、ファンケース1を貫通して送気孔10から気化予
混合室16内に臨んだシャフト5先端にはモータ4側よ
り、シャフト5先端に向けて径が大きくなる円垂台形状
のコーン26、回転板27、周端に攪拌用小羽25上方
に開口するように設置しである。
On the other hand, at the tip of the shaft 5 that passes through the fan case 1 and faces into the vaporizing premixing chamber 16 from the air supply hole 10, there is a cone 26 in the shape of a truncated cone whose diameter increases toward the tip of the shaft 5 from the motor 4 side. The rotating plate 27 is installed at its peripheral end so as to open above the stirring blades 25.

上記構成における動作を説明する。The operation in the above configuration will be explained.

ヒータ14に通電されて気化予混合室16の側壁が所定
の温度に達するとモータ4、電磁ポンプ(図示せず)に
通電されて空気、液体燃料の供給を開始する。液体燃料
は給油管29て回転していケ るツー26上に送られ、コーン26のテーパに沿って流
れ回転板27に達するとその回転力で円周5 。
When the heater 14 is energized and the side wall of the vaporization premixing chamber 16 reaches a predetermined temperature, the motor 4 and the electromagnetic pump (not shown) are energized to start supplying air and liquid fuel. The liquid fuel is sent onto the rotating tool 26 through the fuel supply pipe 29, flows along the taper of the cone 26, and when it reaches the rotary plate 27, its rotational force causes it to rotate around the circumference 5.

方向に飛散され、定温状態に達している気化予混合室1
6壁に接触して気化する。他方、ファン8によって空気
は吸気口6から空気導入口2を経て吸引され、送気口1
oから気化予混合室16内に送り込まれたのち気化した
液体燃料ガスと混合板280作用で均質に混合され予混
合ガスとなる。
Vaporization premixing chamber 1 that is scattered in the direction and reaches a constant temperature state
6 It vaporizes when it comes into contact with the wall. On the other hand, the fan 8 sucks air from the air intake port 6 through the air introduction port 2, and the air is sucked into the air supply port 1.
After being sent into the vaporization premixing chamber 16 from the fuel gas, it is homogeneously mixed with the vaporized liquid fuel gas by the action of the mixing plate 280 to form a premixed gas.

予混合ガスはキ1抗板15整流素子18を通り空間21
内に送られるがここで点火プラグ22のスパーク火花に
よって点火され整流素子18に設けられた多数の小孔を
炎口として多数の小火炎3oを形成し燃焼を行なう。こ
の状態を@2図に示す。
The premixed gas passes through the key 1 resistor plate 15 rectifying element 18 and enters the space 21.
Here, the flame is ignited by the spark of the spark plug 22, and a large number of small flames 3o are formed using the large number of small holes provided in the rectifying element 18 as flame ports, and combustion occurs. This state is shown in Figure @2.

この小火炎30で得られる熱により触媒燃焼層2゜が予
熱されるのである。この段階では送られる空気量、液体
燃料の供給量は整流素子18の小孔に火炎を形成し得る
量に調整されていなくてはならず、空気の場合は吸気口
6の外側に電動で空気流量を調節可能なダンパ(図示せ
ず)を設け、液体燃料の供給量調節には、電磁ポンプ(
図示せず)のパルスを制御することで可能である。整流
素子18の小孔で燃焼する小火炎3oの燃煉後のガス温
度は700〜1oOoCに達し、これによって触媒燃焼
層20が少なくとも700C程度に予熱されると、これ
を燃焼筒13外壁に設けた温度検知素子26が二次的に
検知し、制御回路(図示せず)の切換を行なう。この切
換によって供給される空気量がまずダンパ(図示せず)
の作用で触媒燃焼層20での酸化反応を行なわし得る量
にまで増加させられる。このとき整流素子18上の小火
炎30に対しては空気過剰となり、第3図に示す如くリ
フト火炎31となり最終的には触媒燃焼層20に達した
のち消滅する。一方、液体燃料の供給量は上述の空気量
を増加した時点から適度のタイムラグを設はリフト火炎
31が消滅した後に定常量にまで増加するように制御す
る。以上の操作によって触媒燃焼層20において無火炎
の接触酸化反応による触媒燃焼を定常状態に至らしめる
ことができる。
The heat obtained by this small flame 30 preheats the catalytic combustion layer 2°. At this stage, the amount of air sent and the amount of liquid fuel supplied must be adjusted to an amount that can form a flame in the small holes of the rectifying element 18. A damper (not shown) that can adjust the flow rate is provided, and an electromagnetic pump (
This is possible by controlling pulses (not shown). The gas temperature after combustion of the small flame 3o that burns in the small holes of the rectifying element 18 reaches 700 to 1oOoC, and when the catalytic combustion layer 20 is preheated to at least about 700C, this is installed on the outer wall of the combustion tube 13. The temperature sensing element 26 detects the temperature secondarily and switches the control circuit (not shown). The amount of air supplied by this switching is first applied to the damper (not shown).
As a result of this action, the amount is increased to the extent that the oxidation reaction in the catalytic combustion layer 20 can be carried out. At this time, there is excess air in the small flame 30 on the rectifying element 18, which becomes a lift flame 31 as shown in FIG. 3 and finally reaches the catalytic combustion layer 20 and then disappears. On the other hand, the amount of liquid fuel supplied is controlled so as to increase to a steady amount after the lift flame 31 is extinguished by setting a suitable time lag from the time when the above-mentioned air amount is increased. By the above operations, the catalytic combustion by flameless catalytic oxidation reaction in the catalytic combustion layer 20 can be brought to a steady state.

また、定常の触媒燃焼へ移行した後で下記のよ、うな異
常が生じると触媒燃焼層2oの温度が変化する。
Further, if an abnormality as described below occurs after transition to steady catalytic combustion, the temperature of the catalytic combustion layer 2o changes.

1 触媒燃焼層2oの活性が劣化した場合には、触媒燃
焼層20での酸化反応量が減少し、その結果Coや未燃
焼成分を排気する吹飛び現象を生じ、触媒燃焼層2oの
温度は低下する。
1 When the activity of the catalytic combustion layer 2o deteriorates, the amount of oxidation reaction in the catalytic combustion layer 20 decreases, resulting in a blow-off phenomenon in which Co and unburned components are exhausted, and the temperature of the catalytic combustion layer 2o decreases. descend.

2 空気量が許容変動幅以上に増加した場合には余分の
空気を加熱しなくては々らず、そのため温度の低下を引
起すとともに吹飛びを生じる。
2. If the amount of air increases beyond the permissible fluctuation range, the excess air must be heated, which causes a drop in temperature and causes blow-off.

3 空気量が逆に著しく減少すると触媒燃焼層20を通
過する速度が遅くなシ、触媒燃焼層2゜の整流板18側
での反応量が増加し、また加熱する空気量も少ないため
触媒燃焼層20の温度は上昇し、バックや触媒の劣化を
促進する。
3 On the contrary, if the amount of air decreases significantly, the speed of passing through the catalytic combustion layer 20 will be slow, the amount of reaction on the baffle plate 18 side of the catalytic combustion layer 2 will increase, and the amount of air to be heated will be small, so catalytic combustion will not be possible. The temperature of the layer 20 increases, accelerating deterioration of the bag and catalyst.

4 燃料供給量が許容変動幅以上に増加すると、触媒燃
焼層2oでの発熱量の増加によシ触媒燃焼層2oの温度
は上昇し、熱雰囲気下の反応量増加も加わシ、加速度的
に触媒燃焼層2oの温度を上昇させる。その結果、バン
ク、すなわち、第2図に示した様な火炎燃焼を引起した
シ、触媒活性の劣化、触媒担体の溶融をまねくものであ
る。
4 When the amount of fuel supplied increases beyond the allowable fluctuation range, the temperature of the catalytic combustion layer 2o increases due to the increase in the amount of heat generated in the catalytic combustion layer 2o, and the increase in the amount of reaction in the hot atmosphere is also added. The temperature of the catalytic combustion layer 2o is increased. As a result, this causes a bank, ie, a flame combustion as shown in FIG. 2, deterioration of catalyst activity, and melting of the catalyst carrier.

6 燃料供給量が逆に減少すると発熱量が減少するため
、充分に触媒の活性が生かせずに吹飛びを生じる。即ち
、相対的に2と同様の結果となる。
6 If the amount of fuel supplied decreases, the amount of heat generated decreases, which prevents the catalyst from making full use of its activity, resulting in blow-off. That is, the result is relatively similar to 2.

このように、点火における触媒燃焼層2oの予熱状態や
、定常燃焼時の触媒燃焼層20の状態を把握する上で、
触媒燃焼層2oの温度をモニタすることは装置の構成上
、また安全上極めて有効な手段である。触媒燃焼層2o
の温度を直接測定するのが最も良いが、高温度(7oO
〜1500C)であシ、また、触媒燃焼層2oを構成す
るハニカム体の小孔内に挿入する必要がある。また、酸
化雰囲気に耐えるものでなくてはならない等の条件から
直接測定は困難である。そこで本発明では触媒燃焼層を
固定しである燃焼筒外壁に温度検知素子を取付け、触媒
燃焼層の温度を間接的にモニタするようにしたものであ
る。温度検知素子が燃焼筒外壁に取付けられているため
、異常温度変化に対し士数秒ないし1分程度の遅れが出
るものの上述した異常現象に対しては充分の感応性を有
している。1だ、温度検知素子も耐高温性を特に要求さ
れず、例えばに熱電対、さらには液体封入型のサーモス
タット等を使うことも可能である。本実施例では、触媒
燃焼層温度が最高点で約1100Cのとき温度検知素子
(K熱電対)は約350Cを示していた。
In this way, in understanding the preheating state of the catalytic combustion layer 2o during ignition and the state of the catalytic combustion layer 20 during steady combustion,
Monitoring the temperature of the catalytic combustion layer 2o is an extremely effective means in terms of device configuration and safety. Catalytic combustion layer 2o
Although it is best to directly measure the temperature at
~1500C), and also needs to be inserted into the small holes of the honeycomb body that constitutes the catalytic combustion layer 2o. Furthermore, direct measurement is difficult due to conditions such as the need to withstand an oxidizing atmosphere. Therefore, in the present invention, a temperature sensing element is attached to the outer wall of the combustion cylinder to which the catalytic combustion layer is fixed, so that the temperature of the catalytic combustion layer is indirectly monitored. Since the temperature detection element is attached to the outer wall of the combustion cylinder, it is sufficiently sensitive to the above-mentioned abnormal phenomena, although there is a delay of about a few seconds to one minute in response to abnormal temperature changes. 1. The temperature sensing element is not particularly required to be resistant to high temperatures; for example, a thermocouple or even a liquid-filled thermostat can be used. In this example, when the catalyst combustion layer temperature was about 1100C at the highest point, the temperature detection element (K thermocouple) showed about 350C.

本発明は、触媒燃焼層固定部分の燃焼筒外壁に温度検知
素子を設け、その異常温度変化等を検知して、吹飛びや
バック等の異常を引起した場合には触媒燃焼を停止させ
るなどの安全策を構じることができ、また触媒燃焼層の
予熱完了をも検知し得るなど優れた性能を発揮するもの
である。
The present invention provides a temperature detection element on the outer wall of the combustion cylinder at the part where the catalytic combustion layer is fixed, detects abnormal temperature changes, etc., and stops catalytic combustion when an abnormality such as blow-out or back-up occurs. It exhibits excellent performance, allowing for safety measures and the ability to detect the completion of preheating of the catalytic combustion layer.

本実施例では液体燃料を用いた触媒燃焼装置を示したが
、ガス燃料を用いてもよく、この場合でも適度の空燃比
を有した予混合ガスとして燃焼筒に供給すれば良いもの
である。
In this embodiment, a catalytic combustion device using liquid fuel is shown, but gas fuel may also be used, and even in this case, it is sufficient to supply the combustion cylinder as a premixed gas having an appropriate air-fuel ratio.

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

第1図は本発明の一実施例で液体燃料の触媒燃焼装置の
縦断面図、第2図は、第1図に示した触媒燃焼装置の要
部であって触媒燃焼層予熱時あるいはバックの状態を示
した図、第3図は、第1図の要部であって、触媒燃焼へ
の移行途中を示す状態図である。 13・・・・・・燃焼筒、2o・・・・・・触媒燃焼層
、26・・・・・・温度検知素子。
FIG. 1 is a vertical cross-sectional view of a liquid fuel catalytic combustion device according to an embodiment of the present invention, and FIG. 2 is a main part of the catalytic combustion device shown in FIG. FIG. 3, which shows the state, is a main part of FIG. 1, and is a state diagram showing a state in the middle of transition to catalytic combustion. 13... Combustion cylinder, 2o... Catalytic combustion layer, 26... Temperature detection element.

Claims (1)

【特許請求の範囲】[Claims] ガス状燃料と空気の予混合ガスを供給する手段と、触媒
燃焼層を装着した燃焼筒とを備え、前記予混合ガスを燃
焼筒内の触媒燃焼層に導入して予混合ガスを触媒酸化反
応によって燃焼させる構成とし、触媒燃焼層部分の燃焼
筒外壁に温度検知素子を取付けた触媒燃焼装置。
A means for supplying a premixed gas of gaseous fuel and air and a combustion tube equipped with a catalytic combustion layer are provided, and the premixed gas is introduced into the catalytic combustion layer in the combustion tube to perform a catalytic oxidation reaction on the premixed gas. This catalytic combustion device has a configuration in which combustion is performed using the following methods, and a temperature sensing element is attached to the outer wall of the combustion cylinder in the catalytic combustion layer.
JP16325881A 1981-10-13 1981-10-13 Catalytic combustion equipment Pending JPS5864412A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16325881A JPS5864412A (en) 1981-10-13 1981-10-13 Catalytic combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16325881A JPS5864412A (en) 1981-10-13 1981-10-13 Catalytic combustion equipment

Publications (1)

Publication Number Publication Date
JPS5864412A true JPS5864412A (en) 1983-04-16

Family

ID=15770372

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16325881A Pending JPS5864412A (en) 1981-10-13 1981-10-13 Catalytic combustion equipment

Country Status (1)

Country Link
JP (1) JPS5864412A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1058055A1 (en) * 1998-12-18 2000-12-06 Matsushita Electric Industrial Co., Ltd. Catalyst combustion device
JP2012220089A (en) * 2011-04-08 2012-11-12 Corona Corp Combustion device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52109476A (en) * 1976-03-11 1977-09-13 Ngk Spark Plug Co Deodorization apparatus
JPS5319555B2 (en) * 1971-12-24 1978-06-21
JPS5630514A (en) * 1979-08-20 1981-03-27 Matsushita Electric Ind Co Ltd Liquid fuel combusting apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5319555B2 (en) * 1971-12-24 1978-06-21
JPS52109476A (en) * 1976-03-11 1977-09-13 Ngk Spark Plug Co Deodorization apparatus
JPS5630514A (en) * 1979-08-20 1981-03-27 Matsushita Electric Ind Co Ltd Liquid fuel combusting apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1058055A1 (en) * 1998-12-18 2000-12-06 Matsushita Electric Industrial Co., Ltd. Catalyst combustion device
EP1058055A4 (en) * 1998-12-18 2005-05-18 Matsushita Electric Ind Co Ltd Catalyst combustion device
JP2012220089A (en) * 2011-04-08 2012-11-12 Corona Corp Combustion device

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