JP2806018B2 - Catalytic combustion device - Google Patents

Catalytic combustion device

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Publication number
JP2806018B2
JP2806018B2 JP24079390A JP24079390A JP2806018B2 JP 2806018 B2 JP2806018 B2 JP 2806018B2 JP 24079390 A JP24079390 A JP 24079390A JP 24079390 A JP24079390 A JP 24079390A JP 2806018 B2 JP2806018 B2 JP 2806018B2
Authority
JP
Japan
Prior art keywords
catalyst layer
temperature
auxiliary
combustion
fuel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP24079390A
Other languages
Japanese (ja)
Other versions
JPH04121507A (en
Inventor
正人 保坂
博久 加藤
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 JP24079390A priority Critical patent/JP2806018B2/en
Publication of JPH04121507A publication Critical patent/JPH04121507A/en
Application granted granted Critical
Publication of JP2806018B2 publication Critical patent/JP2806018B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 本発明は触媒燃料装置に関し、特に加熱、暖房、乾燥
等に用いられる気体燃料または液体燃料の触媒燃焼装置
に関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a catalytic fuel device, and more particularly to a catalytic combustion device for gaseous or liquid fuel used for heating, heating, drying and the like.

従来の技術 従来の触媒燃焼装置は第2図に示すような構成になっ
ている。燃料および空気は燃料タンク1に設けたポンプ
2およびファン3により混合室4に供給され、燃料は混
合室4内で気化して空気と混合されたのちに1次燃焼部
5に至り、点火装置6により点火されてここに火炎を形
成する。高温の燃焼排ガスは触媒層7を経て排気口8か
ら排出されるが、その間に触媒層7を加熱昇温させる。
触媒層7が触媒燃料を行なうのに十分な温度に達したこ
とが検出されると(検出部は図示せず)、ポンプ2を停
止し、1次燃焼部5の火炎を消滅させる。この後再度ポ
ンプ2を作動させて燃料を供給すると、1次燃焼部5に
おいては火炎を形成せず予混合ガスのまま、燃料は触媒
層7に到達する。ここで、触媒層7は十分温度が上昇し
ているために、触媒燃焼を開始し、完全燃焼が行なわれ
る。触媒燃焼は触媒層7の上流側側面で専ら進行するか
ら、その部分は輻射放熱体となり、ガラス窓9を透過し
て全面に輻射放熱する。
2. Description of the Related Art A conventional catalytic combustion device has a configuration as shown in FIG. Fuel and air are supplied to a mixing chamber 4 by a pump 2 and a fan 3 provided in a fuel tank 1. The fuel is vaporized in the mixing chamber 4 and mixed with the air, and then reaches a primary combustion section 5, where an ignition device is provided. 6 to form a flame there. The high-temperature combustion exhaust gas is discharged from the exhaust port 8 through the catalyst layer 7, during which the catalyst layer 7 is heated and heated.
When it is detected that the temperature of the catalyst layer 7 has reached a temperature sufficient to supply the catalyst fuel (the detection unit is not shown), the pump 2 is stopped and the flame of the primary combustion unit 5 is extinguished. Thereafter, when the pump 2 is operated again to supply fuel, the fuel reaches the catalyst layer 7 in the primary combustion section 5 without forming a flame and as a premixed gas. Here, since the temperature of the catalyst layer 7 has risen sufficiently, catalytic combustion is started, and complete combustion is performed. Since catalytic combustion proceeds exclusively on the upstream side surface of the catalyst layer 7, that portion becomes a radiation radiator and passes through the glass window 9 to radiate radiation to the entire surface.

発明が解決しようとする課題 触媒燃焼装置は空気と予混合された燃料が触媒層にお
いて酸化反応を生じ、反応熱とともに二酸化炭素や水を
発生する。ここで温度と時間が充分にあれば完全な反応
が行なわれるが。触媒層の周縁部等の低温部分や、予混
合気の過濃あるいは希薄部分と接触した位置では、完全
燃焼できずに燃料の一部(炭化水素以後HCと略記する)
や中間生成物(特にCO)が発生するという課題が生じ
る。
Problems to be Solved by the Invention In a catalytic combustion device, fuel premixed with air causes an oxidation reaction in a catalyst layer, and generates carbon dioxide and water along with reaction heat. Here, if the temperature and time are sufficient, a complete reaction is performed. At a low temperature part such as the peripheral part of the catalyst layer, or at a position where it is in contact with an excessively rich or lean part of the premixed gas, a part of the fuel cannot be completely burned (hereinafter abbreviated as HC after hydrocarbon).
And the generation of intermediate products (especially CO).

特に触媒の活性は熱的劣化を避けることはできず、経
時変化とともに触媒の活性が低下しHCやCOの発生が増加
してくるという課題が生じる。
In particular, the catalytic activity cannot avoid thermal deterioration, and there is a problem that the activity of the catalyst decreases with time and the generation of HC and CO increases.

本発明は上記従来技術の課題を解決し、不完全燃焼を
防止して長期間に亘る清浄な排ガス生成を維持すること
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, prevent incomplete combustion, and maintain clean exhaust gas generation for a long period of time.

課題を解決するための手段 この課題を解決するため本発明の触媒燃焼装置は多数
の連通孔を有する主触媒層の下流に、多数の連通孔を有
する補助触媒層を備え、主触媒層と補助触媒層間に燃料
ガスの冷却部を設けた構成とし、 また他の本発明は補助触媒層近傍に温度検出手段を設
け、温度検出手段からの信号により冷却部の冷却熱量を
制御し、補助触媒層に到達する燃焼ガス温度を制御する
構成としたものである。
Means for Solving the Problems In order to solve this problem, the catalytic combustion device of the present invention includes an auxiliary catalyst layer having a large number of communication holes downstream of a main catalyst layer having a large number of communication holes. In another aspect of the present invention, a temperature detecting means is provided in the vicinity of the auxiliary catalyst layer, and the amount of cooling heat of the cooling section is controlled by a signal from the temperature detecting means. Is configured to control the temperature of the combustion gas reaching the combustion gas.

作用 この構成により本発明の触媒燃料装置は主触媒層の周
縁部等の低温部分や、予混合気の過濃あるいは過希薄部
分と接触した位置では、予混合気は完全燃焼できずに燃
料の一部(HC)や中間生成物(特にCO)が発生する。こ
の主触媒層における燃焼ガス中に含まれるHCやCOを、主
触媒層下流に設けた補助触媒層で完全反応させることと
なる。そして、補助触媒層のの熱的劣化を防止するため
に、主触媒層と補助触媒層間で燃焼ガスを冷却し、燃焼
ガス温度を低くして燃焼ガスを補助触媒層に到達させる
こととなる。
Operation With this configuration, in the catalytic fuel device of the present invention, at a low temperature portion such as the peripheral portion of the main catalyst layer, or at a position where the premixed gas is in contact with an excessively rich or excessively lean portion, the premixed gas cannot be completely burned, and the Some (HC) and intermediate products (especially CO) are generated. HC and CO contained in the combustion gas in the main catalyst layer are completely reacted by the auxiliary catalyst layer provided downstream of the main catalyst layer. Then, in order to prevent the auxiliary catalyst layer from being thermally degraded, the combustion gas is cooled between the main catalyst layer and the auxiliary catalyst layer, the temperature of the combustion gas is lowered, and the combustion gas reaches the auxiliary catalyst layer.

さらに、補助触媒層近傍に温度検出部を設け、温度検
出部からの信号により補助触媒層に到達する燃焼ガス温
度を制御することとなる。
Further, a temperature detector is provided near the auxiliary catalyst layer, and the temperature of the combustion gas reaching the auxiliary catalyst layer is controlled by a signal from the temperature detector.

実施例 以下本発明の一実施例の触媒燃焼装置を添付図面に基
づいて説明する。第1図において10は燃料タンク、11は
燃料供給用ポンプ、12は送風用ファンで両者は混合室13
に連通している。混合室13には加熱用ヒータ(図示せ
ず)を設けている。混合室13下流には1次燃焼部14を備
え、その近傍には点火装置15を設けている。1次燃焼部
14の下流にはハニカム状セラミックからなる主触媒層16
を設け、主触媒層16の下流には補助触媒層17を設け、排
気口22へと連通している。
An embodiment of the present invention will be described below with reference to the accompanying drawings. In FIG. 1, 10 is a fuel tank, 11 is a fuel supply pump, 12 is a blower fan, and both are mixing chambers 13.
Is in communication with The mixing chamber 13 is provided with a heater for heating (not shown). A primary combustion section 14 is provided downstream of the mixing chamber 13, and an ignition device 15 is provided near the primary combustion section 14. Primary combustion section
Downstream of 14 is a main catalyst layer 16 made of a honeycomb-shaped ceramic.
The auxiliary catalyst layer 17 is provided downstream of the main catalyst layer 16 and communicates with the exhaust port 22.

燃料および空気は燃料供給用ポンプ11および送風用フ
ァン12によって混合室13に供給され、燃料は混合室13で
気化して空気と混合された後に1次燃焼部14に至り、点
火装置15により点火されてここに火炎を形成する。高温
の燃焼排ガスは主触媒層16を加熱昇温する。主触媒層16
が触媒燃焼を行なうのに充分な温度に達したことが検出
されると(検出部は図示せず)、燃料供給ポンプ11を停
止し、1次燃焼部14の火炎を消滅させる。この後、再度
燃料供給ポンプ11を作動させて混合室13に燃料を供給す
ると、1次燃焼部14においては火炎を形成せずに、予混
合ガスのまま主触媒層16に到達し、主触媒層16で触媒燃
焼を開始する。
Fuel and air are supplied to a mixing chamber 13 by a fuel supply pump 11 and a blower fan 12, and the fuel is vaporized in the mixing chamber 13 and mixed with air, and then reaches a primary combustion section 14, where it is ignited by an ignition device 15. Being here forms a flame. The high-temperature combustion exhaust gas heats and raises the temperature of the main catalyst layer 16. Main catalyst layer 16
When it is detected that the temperature has reached a temperature sufficient to perform catalytic combustion (the detection unit is not shown), the fuel supply pump 11 is stopped, and the flame of the primary combustion unit 14 is extinguished. Thereafter, when the fuel supply pump 11 is operated again to supply fuel to the mixing chamber 13, the primary combustion portion 14 does not form a flame, but reaches the main catalyst layer 16 as a premixed gas, and In layer 16, catalytic combustion starts.

この時、主触媒層16の周縁部等の低温部分や、予混合
気の過濃あるいは過希薄部分と接触した位置では、予混
合気は完全燃焼できずにHCやCOが発生する。本実施例で
は主触媒層16下流に補助触媒層17を設けているために、
主触媒層16における燃焼ガス中に含まれるHCやCOを、補
助触媒層17で完全反応させて浄化し、清浄な排ガスにす
ることができる。
At this time, in a low temperature portion such as the peripheral portion of the main catalyst layer 16 or a position where the premixed gas is in contact with an excessively rich or excessively lean portion, the premixed gas cannot be completely burned, and HC and CO are generated. In this embodiment, since the auxiliary catalyst layer 17 is provided downstream of the main catalyst layer 16,
HC and CO contained in the combustion gas in the main catalyst layer 16 can be completely reacted and purified in the auxiliary catalyst layer 17 to produce clean exhaust gas.

一般に、触媒の活性は熱的劣化を避けることはでき
ず、経時変化とともに触媒の活性が低下しHCやCOの発生
が増加してくる。触媒の熱的劣化を抑制するためには触
媒層の燃焼温度を低下すればよいが、触媒燃焼器の用途
を考慮すると、一概には触媒層の温度を低下することは
できない。したがって燃焼時間の経過とともに、主触媒
層17から排出される燃焼ガスに含まれるHCやCOの発生量
は増加してくる。この触媒活性の熱的劣化は主触媒層16
ばかりでなく補助触媒層17でも生じる現象である。しか
し、補助触媒層17は主触媒層16で燃焼できなかった微量
のCOやHCを燃焼するためのものであるから、主触媒層16
のように触媒温度を高温にする必要がなく、また触媒燃
焼装置の使用用途からくる触媒温度の制限も受けない。
In general, thermal degradation of the activity of the catalyst cannot be avoided, and the activity of the catalyst decreases with time and the generation of HC and CO increases. In order to suppress the thermal degradation of the catalyst, the combustion temperature of the catalyst layer may be reduced. However, in consideration of the use of the catalyst combustor, the temperature of the catalyst layer cannot be reduced. Therefore, as the combustion time elapses, the generation amount of HC and CO contained in the combustion gas discharged from the main catalyst layer 17 increases. This thermal degradation of the catalyst activity is caused by the main catalyst layer 16.
This phenomenon occurs not only in the auxiliary catalyst layer 17 but also in the auxiliary catalyst layer 17. However, since the auxiliary catalyst layer 17 is for burning a small amount of CO and HC that could not be burned in the main catalyst layer 16, the main catalyst layer 16
As described above, there is no need to raise the temperature of the catalyst, and there is no restriction on the catalyst temperature due to the use of the catalytic combustion device.

そこで本実施例では主触媒層16と補助触媒層17をつな
ぐ燃焼筒18の側面には放熱ファン19からなる冷却部を設
けており、放熱ファン19からの送風により燃焼筒18を強
制的に冷却することにより、主触媒層16からの燃焼ガス
はその温度を低下して、補助触媒層17に到達するように
なる。このため補助触媒層17は高温にならず、燃焼が経
過しても熱的劣化を受けず、主触媒層16から発生するCO
やHCを完全燃焼し、長期間に亘る清浄な排ガス生成を維
持することを可能とした。
Therefore, in the present embodiment, a cooling unit including a radiating fan 19 is provided on a side surface of the combustion tube 18 connecting the main catalyst layer 16 and the auxiliary catalyst layer 17, and the combustion tube 18 is forcibly cooled by blowing air from the radiating fan 19. By doing so, the temperature of the combustion gas from the main catalyst layer 16 decreases, and reaches the auxiliary catalyst layer 17. For this reason, the auxiliary catalyst layer 17 does not reach a high temperature, is not thermally degraded even after the combustion, and the CO generated from the main catalyst layer 16 is reduced.
And HC were completely burned, and it was possible to maintain clean exhaust gas generation for a long period of time.

さらに他の実施例として、第1図に示すように補助触
媒17近傍に温度検出部20を設けると、以下に示すような
作用効果がある。
As yet another embodiment, when the temperature detecting section 20 is provided near the auxiliary catalyst 17 as shown in FIG. 1, the following operation and effect can be obtained.

温度検出部20は本実施例のように補助触媒層17近傍に
設けて燃焼ガス温度を検出しているが、補助触媒層17に
直接接触して取り付けてるなどして、補助触媒層17の温
度を検出してもよい。ここで、温度検出部20は、サーモ
カップル、光センサなどで、温度、光などを検知して、
燃焼ガス温度や補助触媒層17の温度を検出できるもので
ある。本実施例ではサーモカップルを用いている。
Although the temperature detector 20 is provided near the auxiliary catalyst layer 17 to detect the temperature of the combustion gas as in the present embodiment, the temperature of the auxiliary catalyst layer 17 May be detected. Here, the temperature detection unit 20 detects temperature, light, and the like with a thermocouple, an optical sensor, and the like.
The temperature of the combustion gas and the temperature of the auxiliary catalyst layer 17 can be detected. In this embodiment, a thermocouple is used.

温度検出部20からの信号は温度コントローラ21に送ら
れ、燃焼ガス温度や補助触媒層17の温度が設定値になる
ように放熱ファン19の送風量をコントロールする。この
ために補助触媒層17の燃焼温度を精度よくコントロール
することができる。
The signal from the temperature detection unit 20 is sent to the temperature controller 21 to control the amount of air blown by the heat radiating fan 19 so that the combustion gas temperature and the temperature of the auxiliary catalyst layer 17 become set values. Therefore, the combustion temperature of the auxiliary catalyst layer 17 can be controlled accurately.

このために主触媒層16における燃焼負荷の変動にも的
確に対処することができ、補助触媒層17の高温化を抑制
し、補助触媒層17の耐久性を飛躍的に向上することがで
きる。
For this reason, it is possible to appropriately cope with the fluctuation of the combustion load in the main catalyst layer 16, suppress the increase in the temperature of the auxiliary catalyst layer 17, and dramatically improve the durability of the auxiliary catalyst layer 17.

さらに、補助触媒層17に到達する燃焼ガス温度を精度
よくコントロールすることから、補助触媒層17の仕様の
最適化を図ることができる。このため補助触媒層17の容
量を最小限にすることができ、低コストでより効果的に
排ガスを浄化することができる。
Further, since the temperature of the combustion gas reaching the auxiliary catalyst layer 17 is accurately controlled, the specifications of the auxiliary catalyst layer 17 can be optimized. Therefore, the capacity of the auxiliary catalyst layer 17 can be minimized, and the exhaust gas can be more effectively purified at low cost.

上記実施例は石油燃焼について述べたものであるが、
ガス燃料等についても同様な結果が得られており、燃料
種を限定するものではない。また、触媒体の材質や形状
等によっても大きな差異はなく、セラミック繊維の編組
体や金属ハニカム体を用いても同様な結果が得られてい
る。
Although the above example describes oil burning,
Similar results have been obtained for gaseous fuel and the like, and the fuel type is not limited. Further, there is no significant difference depending on the material and shape of the catalyst body, and similar results are obtained by using a braided ceramic fiber body or a metal honeycomb body.

発明の効果 以上の実施例の説明で明らかなように本発明の触媒燃
焼装置によれば多数の連通孔を有する主触媒層の下流
に、多数の連通孔を有する補助触媒層を備え、主触媒層
と補助触媒層間に燃焼ガスの冷却部を設けることによ
り、不完全燃焼を防止して長期間に亘る清浄な排ガス生
成を維持することができる。
Effects of the Invention As is apparent from the above description of the embodiment, according to the catalytic combustion device of the present invention, the auxiliary catalyst layer having a large number of communication holes is provided downstream of the main catalyst layer having a large number of communication holes, By providing a cooling portion for the combustion gas between the layer and the auxiliary catalyst layer, incomplete combustion can be prevented and clean exhaust gas generation can be maintained for a long period of time.

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

第1図は本発明の一実施例における触媒燃焼器の側断面
図、第2図は従来の触媒燃焼装置の側断面図である。 13……混合室、16……主触媒層、17……補助触媒層、19
……放熱ファン、20……温度検出部。
FIG. 1 is a sectional side view of a catalytic combustor according to an embodiment of the present invention, and FIG. 2 is a sectional side view of a conventional catalytic combustion device. 13 ... mixing chamber, 16 ... main catalyst layer, 17 ... auxiliary catalyst layer, 19
…… a heat dissipation fan, 20 …… a temperature detector.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F23D 11/40 F23C 11/00 306 F23C 11/00 312──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) F23D 11/40 F23C 11/00 306 F23C 11/00 312

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】燃料と空気の混合室と、前記混合室の下流
に備えられた多数の連通孔を有する主触媒層と、前記主
触媒層の下流に備えられた多数の連通孔を有する補助触
媒層とを備え、前記主触媒層と前記補助触媒層の間に燃
焼ガスの冷却部を設けてなる触媒燃焼装置。
1. A fuel / air mixing chamber, a main catalyst layer having a plurality of communication holes provided downstream of the mixing chamber, and an auxiliary having a plurality of communication holes provided downstream of the main catalyst layer. A catalytic combustion apparatus comprising: a catalyst layer; and a combustion gas cooling unit provided between the main catalyst layer and the auxiliary catalyst layer.
【請求項2】燃料と空気の混合室と、前記混合室の下流
に備えられた多数の連通孔を有する主触媒層と、前記主
触媒層の下流に備えられた多数の連通孔を有する補助触
媒層とを備え、前記主触媒層と前記補助触媒層間に燃焼
ガスの冷却部を設け、前記補助触媒層近傍に温度検出部
を設け、前記温度検出部からの信号により前記補助触媒
層に到達する燃焼ガス温度を制御する触媒燃焼装置。
2. A fuel / air mixing chamber, a main catalyst layer having a plurality of communication holes provided downstream of the mixing chamber, and an auxiliary having a plurality of communication holes provided downstream of the main catalyst layer. A catalyst layer, a cooling unit for combustion gas is provided between the main catalyst layer and the auxiliary catalyst layer, a temperature detection unit is provided near the auxiliary catalyst layer, and reaches the auxiliary catalyst layer by a signal from the temperature detection unit. A catalytic combustion device that controls the temperature of the combustion gas.
JP24079390A 1990-09-10 1990-09-10 Catalytic combustion device Expired - Fee Related JP2806018B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24079390A JP2806018B2 (en) 1990-09-10 1990-09-10 Catalytic combustion device

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Application Number Priority Date Filing Date Title
JP24079390A JP2806018B2 (en) 1990-09-10 1990-09-10 Catalytic combustion device

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JPH04121507A JPH04121507A (en) 1992-04-22
JP2806018B2 true JP2806018B2 (en) 1998-09-30

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JP24079390A Expired - Fee Related JP2806018B2 (en) 1990-09-10 1990-09-10 Catalytic combustion device

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JPH04121507A (en) 1992-04-22

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