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JP2567992B2 - Catalytic combustion device - Google Patents
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JP2567992B2 - Catalytic combustion device - Google Patents

Catalytic combustion device

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Publication number
JP2567992B2
JP2567992B2 JP2340179A JP34017990A JP2567992B2 JP 2567992 B2 JP2567992 B2 JP 2567992B2 JP 2340179 A JP2340179 A JP 2340179A JP 34017990 A JP34017990 A JP 34017990A JP 2567992 B2 JP2567992 B2 JP 2567992B2
Authority
JP
Japan
Prior art keywords
catalyst
combustion
heat
catalytic combustion
cylinder
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
JP2340179A
Other languages
Japanese (ja)
Other versions
JPH04350419A (en
Inventor
安昭 坂根
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.)
Sharp Corp
Original Assignee
Sharp 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 Sharp Corp filed Critical Sharp Corp
Priority to JP2340179A priority Critical patent/JP2567992B2/en
Publication of JPH04350419A publication Critical patent/JPH04350419A/en
Application granted granted Critical
Publication of JP2567992B2 publication Critical patent/JP2567992B2/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、遠赤外線放射効率に優れた酸化触媒を応用
し、暖房、乾燥等に用いられる触媒燃焼装置に関するも
のである。
TECHNICAL FIELD The present invention relates to a catalytic combustion apparatus which is used for heating, drying, etc. by applying an oxidation catalyst excellent in far infrared radiation efficiency.

〔従来の技術〕[Conventional technology]

気体燃料及び気化された液体燃料を空気と混合させた
後に触媒層へ送って触媒と接触させ、その表面上で無炎
燃焼させる触媒燃焼装置は、窒素酸化物の放出がなく、
触媒層から放射される遠赤外線の効果でマイルドな輻射
暖房を実現する等の優れた特徴を有するため、従来より
種々提案され、一部は実用化されている。
A catalytic combustion device in which a gaseous fuel and a vaporized liquid fuel are mixed with air and then sent to a catalyst layer to be in contact with a catalyst and flamelessly burned on the surface thereof does not emit nitrogen oxides,
Since it has excellent features such as realizing mild radiant heating by the effect of far infrared rays radiated from the catalyst layer, various proposals have been conventionally made and some of them have been put to practical use.

従来より、このような触媒燃焼装置のうち、担体に耐
熱無機材料を用いて触媒層から生じる輻射熱を利用する
ものの1例として、出願人が提案した第3図(a),
(b)に示すような構造の触媒燃焼装置がある。第3図
(a),(b)によって説明すると、1は触媒層、10は
1次空気調整孔、11は予熱用バーナ、12は気化器、13は
2次空気孔、15は送風機、23は点火用ヒータ、25は温度
センサーである。このように比較的広い面積の触媒層1
の一枚板を触媒層の後方から前方へ予混合ガスが通過す
るように垂直方向に立て、送風機15を運転すると同時に
触媒層の背面から予熱用バーナ11に点火用ヒータ23で点
火して火炎燃焼を行い、この燃焼熱で触媒層1を加熱
し、触媒層が層火温度(活性化温度)以上に達した時点
で予熱用バーナの火炎を消火し、直ちに気化灯油と1次
空気調整孔10からの1次空気及び2次空気孔13からの2
次空気を混合してなる予混合ガスを触媒層1へ供給して
触媒燃焼を開始する構造となっている。この時、触媒層
の広い出口面を輻射に利用するものである。
FIG. 3 (a) proposed by the applicant of the present invention has been proposed as an example of a conventional catalytic combustion apparatus that utilizes radiant heat generated from a catalyst layer by using a heat-resistant inorganic material for a carrier.
There is a catalytic combustion device having a structure as shown in FIG. Referring to FIGS. 3 (a) and 3 (b), 1 is a catalyst layer, 10 is a primary air adjusting hole, 11 is a preheating burner, 12 is a carburetor, 13 is a secondary air hole, 15 is a blower, 23 Is an ignition heater, and 25 is a temperature sensor. Thus, the catalyst layer 1 having a relatively large area
The single plate is erected vertically so that the premixed gas passes from the rear side to the front side of the catalyst layer, and the blower 15 is operated, and at the same time, the preheating burner 11 is ignited by the ignition heater 23 from the back side of the catalyst layer and the flame is emitted. Combustion is performed, the catalyst layer 1 is heated by this combustion heat, and when the catalyst layer reaches the flame temperature (activation temperature) or higher, the flame of the preheating burner is extinguished, and immediately vaporized kerosene and the primary air adjusting hole Primary air from 10 and 2 from secondary air holes 13
The structure is such that a premixed gas obtained by mixing the following air is supplied to the catalyst layer 1 to start catalytic combustion. At this time, the wide exit surface of the catalyst layer is used for radiation.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

上記した従来構成の触媒燃焼装置に於いては、下記の
ごとく欠点があった。
The above-mentioned conventional catalytic combustion apparatus has the following drawbacks.

通常、同一体積の触媒層について、一定の空気比のま
まで燃焼量を絞り、触媒単位面積当たりの燃焼負荷量で
ある面負荷を低下させると触媒層の燃焼温度が低下す
る。また、燃焼用空気量を一定のまま燃焼量のみを絞る
と触媒層の燃焼温度はさらぬ急激に低下する。つまり、
最高燃焼量時に触媒層が赤熱状態で燃焼するのに対して
最低燃焼量時に触媒層は赤熱状態に達せず、常温状態と
同等の外観で燃焼する。このような最低燃焼量時におい
ては、ユーザーが燃焼状態にあるか否かを目視により簡
便に認識し難いために不安感を抱かせやすく、視覚効果
も乏しい。
Normally, for a catalyst layer having the same volume, if the combustion amount is reduced while maintaining a constant air ratio and the surface load, which is the combustion load per unit area of the catalyst, is reduced, the combustion temperature of the catalyst layer decreases. Further, if only the combustion amount is reduced while keeping the combustion air amount constant, the combustion temperature of the catalyst layer will drastically decrease. That is,
At the time of the maximum combustion amount, the catalyst layer burns in a red-hot state, whereas at the time of the minimum combustion amount, the catalyst layer does not reach the red-hot state and burns with the same appearance as that of a normal temperature state. At such a minimum combustion amount, since it is difficult for the user to easily visually recognize whether or not the combustion state is present, it is easy to cause anxiety and the visual effect is poor.

従来より最低燃焼量時においても触媒層を赤熱状態と
するためには、触媒層の負荷面積を小さくすると同時に
予混合ガスの流れ方向の厚みを増して面負荷を大きくす
る必要があった。しかし、このような方法の場合、輻射
利用面である出口面の負胃面積が小さいために輻射熱量
が小さくなるという弊害が生じる。
In order to bring the catalyst layer into a red heat state even at the minimum combustion amount, it has been necessary to reduce the load area of the catalyst layer and at the same time increase the thickness of the premixed gas in the flow direction to increase the surface load. However, in the case of such a method, there is an adverse effect that the amount of radiant heat becomes small because the negative stomach area of the exit surface, which is the radiation utilization surface, is small.

また、従来構造の場合、触媒層の負荷面積が大きいた
め予熱動作時に均一に加熱することが困難であり、予混
合ガスを送って触媒燃焼を開始する時に温度が低い部分
から未燃ガスを排出しやすい。
Further, in the case of the conventional structure, it is difficult to uniformly heat the catalyst layer during the preheating operation because the load area of the catalyst layer is large, and when the premixed gas is sent to start the catalytic combustion, the unburned gas is discharged from the low temperature portion. It's easy to do.

〔課題を解決するための手段〕[Means for solving the problem]

本発明に係る触媒燃焼装置は、上記の課題を解決する
ためになされたものであり、小さな体積の円柱状あるい
は角柱状でハリカム等の通気性に優れた断面形状をもつ
触媒ペレット複数個を耐熱性ガラス筒の中に挿入し、さ
らにこの触媒ペレット最下部にハニカム等の通気性に優
れた形状に成型した抵抗発熱性無機材料を電極と共に挿
入して触媒燃焼筒とし、この触媒燃焼筒を1個若しくは
複数個を立てて下部から予混合ガスを供給するように流
路を形成し、触媒燃焼筒の背後に触媒ペレットから放射
される赤外線を耐熱性ガラスを通して前面に反射させる
ための反射板を配設したものである。
The catalytic combustion apparatus according to the present invention is made to solve the above problems, and heat-treats a plurality of catalyst pellets having a small volume, such as a columnar shape or a prismatic shape, having a cross-sectional shape with excellent breathability such as a hole cam. Of the resistance heat-generating inorganic material, such as a honeycomb, which is molded into a shape having excellent air permeability, is inserted into the lowermost part of the catalyst pellet together with the electrode to form a catalytic combustion cylinder. A flow path is formed so that the premixed gas is supplied from the bottom by standing up one or more pieces, and a reflective plate for reflecting the infrared rays emitted from the catalyst pellets through the heat-resistant glass to the front side behind the catalyst combustion cylinder. It is arranged.

〔作 用〕[Work]

上記の構成に於いて、触媒層の予熱動作時には触媒燃
焼筒下部の抵抗発熱性無機材料に通電を行って発熱させ
ることによりその上部に配設された触媒ペレットを熱伝
導及び自然対流伝熱によって効率良く予熱することがで
き、素早く予熱が完了する。また、触媒燃焼筒1本の負
荷面積が小さいので触媒断面での均熱化も良好であり、
未燃ガスを排出することなく確実に定常燃焼へ移行でき
る。定常燃焼時には、触媒層の負荷面積が従来構造の場
合よりも小さいため、燃焼量が小さい場合でも触媒ペレ
ット入り口部を赤熱状態に保つことができ、この赤熱部
は燃焼量に比例して上方向へ拡大するためいかなる燃焼
量においてもユーザーが燃焼状態を耐熱性ガラスを通し
て目視により簡敏に認識することができる。同時に、燃
焼によって高温となった触媒ペレットの側面から放射さ
れる赤外線を耐熱性ガラス筒を通し、反射板によって前
方へ反射させるため、大きな輻射面積の快適な輻射暖房
が行える。また、小さな触媒ペレット及び予熱用抵抗発
熱性無機材料の集合体で構成されるため個々の成型が容
易でありコストが安くなる。
In the above structure, during the preheating operation of the catalyst layer, the resistance heating inorganic material under the catalyst combustion cylinder is energized to generate heat, so that the catalyst pellets disposed above the catalyst pellet are heated by heat conduction and natural convection heat transfer. Preheating can be done efficiently and preheating is completed quickly. In addition, since the load area of one catalyst combustion cylinder is small, soaking in the catalyst cross section is also good,
It is possible to reliably shift to steady combustion without discharging unburned gas. During steady combustion, the load area of the catalyst layer is smaller than that of the conventional structure, so even if the combustion amount is small, the catalyst pellet inlet can be kept in a red heat state. Therefore, the user can easily visually recognize the combustion state through the heat-resistant glass regardless of the amount of combustion. At the same time, infrared rays radiated from the side surfaces of the catalyst pellets that have become hot due to combustion pass through the heat-resistant glass tube and are reflected forward by the reflector, so that comfortable radiant heating with a large radiant area can be performed. Further, since it is composed of a small catalyst pellet and an aggregate of preheating resistance heating inorganic material, individual molding is easy and the cost is low.

〔実施例〕〔Example〕

本発明の一実施例を第1図、第2図に基づいて説明す
れば以下の通りである。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.

本発明に係る触媒燃焼装置においえ、第1図及び第2
図に示すように、1Aは触媒燃焼筒であり1本もしくは複
数本が垂直方向に立っている。2Aはディフューザ室であ
り触媒燃焼筒1を下部から堅く支持するとともに底面開
口部から送られる予混合ガスを触媒燃焼筒へ通過する天
井開口部へ均等に供給する箱難室である。3Aは混合室で
あり図示しない送油ポンプより送油パイプ4Aを通って送
られる燃料を送風機5Aより圧送される燃焼用空気と混合
して予混合ガスを生成する。尚、燃料が液体燃料の場合
は混合室3Aの中に燃料気化のためのヒータが設置されて
いる。6Aは廃棄ダクトであり触媒燃焼筒1Aを上部で堅く
支持するとともに触媒燃焼筒に通過する底面開口部から
送られる燃焼ガスを集めて上面開口部から大気中へ排出
する箱難室である。触媒燃焼筒1Aは主に、熱透過率に優
れた筒状耐熱性ガラス筒12Aと、円柱状もしくは角柱状
で断面がハニカム構造等の通気性に優れた形状に成型し
たコージュライト等の耐熱性無機材料を担体として用い
この表面に白金族金属等の酸化触媒を担持して成る触媒
ペレット11A数個及び触媒ペレットと同形状で炭化珪素
等の抵抗発熱性無機材料によって成型された予熱用ヒー
タ13Aの1個から成り、耐熱性ガラス筒12Aの中に入口側
最上流部に予熱用ヒータ13Aがまたその上部下流側には
数個の触媒ペレット11Aが積み重ねて挿入されている。
予熱用ヒータ13Aの外周2箇所には電圧を印加するため
の電極が取り付けられており、その下端部のディフュー
ザ室2Aとの接続部は絶縁シール剤によって絶縁保持され
ている。16Aは温度センサーでありそれぞれの触媒燃焼
筒の最上部に取り付けられている。7Aはガード網であり
運転時に高温となる触媒燃焼筒1を託って安全性を確保
する。8Aは反射板でありキャビネット9A内で触媒燃焼筒
1Aの背後を囲むように配置されている。10Aは温風口で
ありキャビネット9の天井に位置し、排気ダクト6Aから
排出される熱風を上方へ排出する。
In the catalytic combustion device according to the present invention, FIG.
As shown in the figure, 1A is a catalytic combustion cylinder, and one or more of them are vertically standing. Reference numeral 2A denotes a diffuser chamber, which is a box difficult chamber that firmly supports the catalytic combustion cylinder 1 from the lower portion and evenly supplies the premixed gas sent from the bottom opening to the ceiling opening that passes to the catalytic combustion cylinder. Reference numeral 3A denotes a mixing chamber, which mixes the fuel sent from an oil sending pump (not shown) through the oil sending pipe 4A with the combustion air sent under pressure from the blower 5A to generate a premixed gas. When the fuel is liquid fuel, a heater for vaporizing the fuel is installed in the mixing chamber 3A. Reference numeral 6A denotes a waste duct, which is a box difficulty chamber that firmly supports the catalytic combustion cylinder 1A at the upper portion and collects the combustion gas sent from the bottom opening passing through the catalytic combustion cylinder and discharges it into the atmosphere from the upper opening. The catalytic combustion cylinder 1A is mainly composed of a cylindrical heat-resistant glass cylinder 12A having excellent heat transmission rate and a heat resistance such as cordierite molded into a shape having a columnar or prismatic shape and a honeycomb structure or the like with excellent air permeability. A catalyst pellet 11A having an inorganic material as a carrier and carrying an oxidation catalyst such as a platinum group metal on its surface, and a preheating heater 13A formed by a resistance heating inorganic material such as silicon carbide in the same shape as the catalyst pellet. In the heat-resistant glass tube 12A, the preheating heater 13A is inserted in the most upstream side of the inlet side, and several catalyst pellets 11A are inserted in the upper downstream side.
Electrodes for applying a voltage are attached to two locations on the outer circumference of the preheating heater 13A, and the lower end portion of the connection portion with the diffuser chamber 2A is insulated and held by an insulating sealant. 16A is a temperature sensor and is attached to the top of each catalytic combustion cylinder. 7A is a guard net, which secures safety by entrusting the catalytic combustion cylinder 1 that becomes hot during operation. 8A is a reflector plate, and a catalytic combustion tube in cabinet 9A
It is arranged to surround the back of 1A. A hot air outlet 10A is located on the ceiling of the cabinet 9 and discharges hot air discharged from the exhaust duct 6A upward.

上記構成を有する触媒燃焼装置の動作は、触媒燃焼に
先立って触媒層を着火温度以上に加熱する予熱動作と、
着火温度に達した触媒層に一定燃焼量の予混合ガスを送
って触媒燃焼を開始し任意の燃焼量の予混合ガスを触媒
層内で無炎燃焼させる定常燃焼動作とから構成される。
The operation of the catalytic combustion device having the above configuration includes a preheating operation of heating the catalyst layer to an ignition temperature or higher prior to catalytic combustion,
It consists of a steady combustion operation in which a fixed combustion amount of the premixed gas is sent to the catalyst layer that has reached the ignition temperature to start catalytic combustion, and an arbitrary combustion amount of the premixed gas is flamelessly burned in the catalyst layer.

予熱動作においては、まず、予熱用ヒータ13Aに通電
を行う。通電により予熱用ヒータが発熱し、その直上の
触媒ペレットから次第に上方の触媒ペレットへと熱伝導
及び自然対流により伝熱を行う。こうしてそれぞれの触
媒燃焼筒に取り付けられた温度センサー16Aのいずれも
が触媒ペレット温度が着火温度(例えば300℃)に達し
たと前記の温度センサー16Aの出力に基づいて図示しな
いコントロールユニットが判断したら、予熱用ヒータへ
の通電を停止し、同時に送風機5Aにより弱送風を開始す
ると共に燃料パイプから燃料供給を開始して混合室3Aで
予混合ガスを生成し、ディフューザ室2Aへ送る。ディフ
ューザ室2Aで予混合ガスは均一に流路を広げて触媒燃焼
筒1Aへ送られ、触媒燃焼を開始する。即ち、予熱動作を
終了し、定常燃焼動作へと移行する。
In the preheating operation, first, the preheating heater 13A is energized. The preheating heater generates heat due to the energization, and heat transfer and natural convection gradually transfer from the catalyst pellet immediately above to the catalyst pellet above. In this way, if the control unit (not shown) determines based on the output of the temperature sensor 16A that the temperature of the catalyst pellets of all the temperature sensors 16A attached to the respective catalyst combustion tubes has reached the ignition temperature (for example, 300 ° C.), The energization of the preheating heater is stopped, at the same time weak air blowing is started by the blower 5A, and fuel supply is started from the fuel pipe to generate premixed gas in the mixing chamber 3A and send it to the diffuser chamber 2A. In the diffuser chamber 2A, the premixed gas is evenly spread over the flow path and sent to the catalytic combustion cylinder 1A to start catalytic combustion. That is, the preheating operation is terminated and the steady combustion operation is started.

触媒ペレット集合体は設定された燃焼量ならばいかな
る燃焼量の予混合ガスでも完全燃焼するのに十分な空間
速度を与える体積に設計されているため、CO,HC等の臭
気ガスを排出することなく着火→昇温→定常弱燃焼へと
移行し、上流側触媒ペレットが赤熱状態(650〜750℃)
で温度が安定状態に達する。また、定常燃焼時には、燃
料送出量及び送風機5Aの送風量を制御し、常に予混合ガ
ウの理論空気量に対する燃焼用供給空気量の体積比(即
ち空気比)を2〜4程度とし、かう触媒ペレット11Aの
最高温度が800℃を越えないように温度センサー16Aを用
いて常に燃焼量に対して適切な送風量に制御することに
より、予混合ガスの逆火及び不完全燃焼を防止しつつ燃
焼量を増減させることができる。このとき、触媒ペレッ
トは低燃焼量時には上流側に近い極一部分だけが赤熱状
態になるのに対して燃焼量の増大とともに赤熱部が上方
へ拡大する。完全燃焼した排気ガスは、触媒ペレット11
Aから排出した後、排気ダクト6Aを通り、温風風10Aより
温風として放出される。一方、触媒ペレットからは、耐
熱性ガラス筒12Aを介して赤外線が放射される。従っ
て、前記の温風による対流暖房と赤外線による輻射暖房
とが同時に行われることになる。
Since the catalyst pellet aggregate is designed to have a volume that gives a sufficient space velocity to completely burn any premixed gas of any combustion amount with a set combustion amount, discharge odorous gases such as CO and HC. Without ignition → temperature rise → transition to steady weak combustion, upstream catalyst pellets red heat (650 to 750 ℃)
The temperature reaches a stable state. Further, at the time of steady combustion, the fuel delivery amount and the air delivery amount of the blower 5A are controlled, and the volume ratio (ie, air ratio) of the combustion supply air amount to the theoretical air amount of the premixing gau is constantly set to about 2 to 4, and the fusing catalyst is used. Combustion is performed while preventing backfire and incomplete combustion of the premixed gas by constantly controlling the air flow rate appropriate for the combustion amount using the temperature sensor 16A so that the maximum temperature of the pellet 11A does not exceed 800 ° C. The amount can be increased or decreased. At this time, when the combustion amount of the catalyst pellet is low, only a part of the catalyst pellet near the upstream side is in a red heat state, whereas the red heat portion expands upward as the combustion amount increases. Exhaust gas that has been completely burned is the catalyst pellet 11
After being discharged from A, it passes through the exhaust duct 6A and is discharged as warm air from the warm air 10A. On the other hand, infrared rays are emitted from the catalyst pellets through the heat-resistant glass tube 12A. Therefore, the convection heating by the warm air and the radiant heating by the infrared rays are simultaneously performed.

消火時には、送風機5Aを除く他の機器への通電を遮断
し、送風機5Aのみを数十秒間作動させ送風を行い、触媒
燃焼筒を主とするシステムの冷却を行う。このとき、触
媒ペレットは比較的大きな熱容量を持つため、予混合ガ
スの供給を急に遮断しても通常の火炎を伴う燃焼のよう
に消火後しばらくCO,HC等の臭気ガスを排出することな
く、触媒ペレット上において完全に酸化される。
At the time of fire extinguishing, the power supply to other devices except the blower 5A is cut off, only the blower 5A is operated for several tens of seconds to blow air, and the system mainly including the catalytic combustion cylinder is cooled. At this time, since the catalyst pellets have a relatively large heat capacity, even if the supply of premixed gas is suddenly cut off, odorous gases such as CO and HC will not be emitted for a while after extinguishing as in combustion with ordinary flames. , Is completely oxidized on the catalyst pellets.

〔発明の効果〕〔The invention's effect〕

本発明に係る触媒燃焼装置は、小さな体積の円柱状あ
るいは角柱状のハニカム断面触媒ペレット複数個を耐熱
性ガラス筒の中に挿入し、さらにこの触媒ペレット最下
部にハニカム等の通気性に優れた形状に成型した抵抗発
熱性無機材料を電極と共に挿入して触媒燃焼筒とし、こ
の触媒燃焼筒を1個若しくは複数個を立てて下部から予
混合ガスを供給するように流路を形成し、触媒燃焼筒の
背後に触媒ペレットから放射される赤外線を耐熱性ガラ
スを通して前面に反射させるための反射板を配設したも
のである。これにより、以下の諸効果を奏する。
The catalytic combustion apparatus according to the present invention has a plurality of small-volume columnar or prismatic honeycomb cross-section catalyst pellets inserted into a heat-resistant glass tube, and further has excellent air permeability such as honeycomb at the bottom of the catalyst pellets. A resistive heating inorganic material molded into a shape is inserted together with an electrode to form a catalytic combustion cylinder, and one or more catalytic combustion cylinders are erected to form a flow path so as to supply a premixed gas from the lower part. A reflection plate for reflecting infrared rays emitted from the catalyst pellets through the heat-resistant glass to the front side is disposed behind the combustion cylinder. This produces the following effects.

(1) 燃焼量に比例して触媒ペレットの赤熱部が流れ
方向に拡大するため、ユーザーにとって燃焼状態を耐熱
性ガラス筒を通して目視により簡便に確認でき、運転時
の不安感を抱かせることがない。また、触媒ペレット側
面からの輻射熱を耐熱性ガラス煤を通して反射板により
前方へ反射させるための大きな輻射熱量が得られる。
(1) Since the red heat part of the catalyst pellet expands in the flow direction in proportion to the amount of combustion, the user can easily visually check the combustion state through the heat-resistant glass tube and do not feel uneasy during operation. . Further, a large amount of radiant heat for reflecting the radiant heat from the side surface of the catalyst pellet through the heat-resistant glass soot to the front by the reflecting plate can be obtained.

(2) 触媒層の予熱動作時には触媒燃焼筒下部の抵抗
発熱無機材料に通電を行って発熱させることによりその
上部に配設された触媒ペレットを熱伝導及び自然対流伝
熱によって効率良く予熱することができ、素早く予熱か
完了する。また、予熱する触媒層の面積が小さいため、
予熱時の触媒ペレット断面における均熱化が容易であ
り、未燃ガスを排出する事なく確実に定常燃焼へ移行で
きる。
(2) During the preheating operation of the catalyst layer, the resistance heating inorganic material in the lower part of the catalyst combustion cylinder is energized to generate heat, so that the catalyst pellets arranged above the catalyst pellet are efficiently preheated by heat conduction and natural convection heat transfer. Can be preheated or completed quickly. Also, since the area of the catalyst layer to be preheated is small,
It is easy to equalize the temperature on the cross section of the catalyst pellet during preheating, and it is possible to reliably shift to steady combustion without discharging unburned gas.

(3) 小さな触媒ペレット及び予熱用抵抗発熱性無機
材料の集合体で構成されるため個々の成型が容易であり
コストが安くなる。
(3) Since it is composed of an aggregate of small catalyst pellets and a resistance heating inorganic material for preheating, individual molding is easy and the cost is low.

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

第1図は本発明の一実施例を示す全体図、第2図は触媒
燃焼筒断面図である。第3図(a),(b)は従来例を
示すもので平面図、側面図である。 1Aは触媒燃焼筒、3Aは混合室、5Aは送風機、10Aは温風
口、11Aは触媒ペレット、12Aは耐熱性ガラス、13Aは予
熱用ヒータ、16Aは温度センサーである。
FIG. 1 is an overall view showing an embodiment of the present invention, and FIG. 2 is a sectional view of a catalytic combustion cylinder. 3 (a) and 3 (b) show a conventional example and are a plan view and a side view. 1A is a catalytic combustion tube, 3A is a mixing chamber, 5A is a blower, 10A is a hot air inlet, 11A is catalyst pellets, 12A is heat-resistant glass, 13A is a preheating heater, and 16A is a temperature sensor.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】気体燃料或は気化した液体燃料を燃焼用空
気と混合させて予混合ガスとなし、触媒層へ送って無炎
燃焼させる触媒燃焼装置において、ハニカム等の通気性
に優れた酸化触媒層を小さな円柱状若しくは角柱状に成
型したものを触媒ペレットとし、熱透過性に優れた耐熱
性ガラス筒の中に触媒ペレットを複数個挿入して成る触
媒燃焼筒を1個若しくは複数個立ててこの中を予混合ガ
スが下方から通過するよう流路を構成し、触媒ペレット
側面からの輻射熱を耐熱性ガラス筒を通して前方へ反射
させる反射板を触媒燃焼筒背後に配設したことを特徴と
する触媒燃焼装置。
1. A catalytic combustion apparatus for mixing a gaseous fuel or a vaporized liquid fuel with combustion air to form a premixed gas, and sending the mixture to a catalyst layer for flameless combustion to oxidize a honeycomb or the like having excellent air permeability. A catalyst cylinder is formed by molding a catalyst layer into a small columnar shape or a prismatic shape, and one or more catalyst combustion cylinders are formed by inserting a plurality of catalyst pellets into a heat-resistant glass cylinder with excellent heat permeability. The flow path is configured so that the premixed gas passes through the lever from below, and a reflector for reflecting the radiant heat from the side surface of the catalyst pellet forward through the heat-resistant glass cylinder is arranged behind the catalyst combustion cylinder. Catalytic combustion device.
【請求項2】前記触媒燃焼筒内の触媒ペレット下部に触
媒ペレットと同一外形でハニカム等の通気性に優れた断
面形状に成型した抵抗発熱性無機材料を予熱用ヒータと
して配設したことを特徴とする特許請求の範囲第一項記
載の触媒燃焼装置。
2. A resistance heating inorganic material formed into a cross-sectional shape having the same outer shape as that of the catalyst pellet, which is excellent in air permeability, is disposed as a preheating heater below the catalyst pellet in the catalyst combustion cylinder. The catalytic combustion device according to claim 1.
JP2340179A 1990-11-30 1990-11-30 Catalytic combustion device Expired - Fee Related JP2567992B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2340179A JP2567992B2 (en) 1990-11-30 1990-11-30 Catalytic combustion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2340179A JP2567992B2 (en) 1990-11-30 1990-11-30 Catalytic combustion device

Publications (2)

Publication Number Publication Date
JPH04350419A JPH04350419A (en) 1992-12-04
JP2567992B2 true JP2567992B2 (en) 1996-12-25

Family

ID=18334479

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2340179A Expired - Fee Related JP2567992B2 (en) 1990-11-30 1990-11-30 Catalytic combustion device

Country Status (1)

Country Link
JP (1) JP2567992B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101688894B1 (en) * 2016-08-08 2016-12-23 주식회사 지엔티엔에스 Using high temperature catalytic combustion burners

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000291917A (en) * 1999-04-07 2000-10-20 Sasakura Engineering Co Ltd Hydrogen combustion treatment device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101688894B1 (en) * 2016-08-08 2016-12-23 주식회사 지엔티엔에스 Using high temperature catalytic combustion burners
WO2018030604A1 (en) * 2016-08-08 2018-02-15 주식회사 지엔티엔에스 Burner using high-temperature combustion catalyst

Also Published As

Publication number Publication date
JPH04350419A (en) 1992-12-04

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