JPS59153017A - Catalytic burner - Google Patents
Catalytic burnerInfo
- Publication number
- JPS59153017A JPS59153017A JP2791483A JP2791483A JPS59153017A JP S59153017 A JPS59153017 A JP S59153017A JP 2791483 A JP2791483 A JP 2791483A JP 2791483 A JP2791483 A JP 2791483A JP S59153017 A JPS59153017 A JP S59153017A
- Authority
- JP
- Japan
- Prior art keywords
- plate
- spouting
- flame hole
- flame
- hole plate
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C13/00—Apparatus 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)
- Spray-Type Burners (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、各種ガス燃料または気化された液体21:、
−ジ
燃料を燃焼空気と共に触媒体上に供給し、その面上にて
酸化反応を起こさせて触媒体を発熱させ、発生した熱を
利用する触媒燃焼器に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is applicable to various gaseous fuels or vaporized liquids 21:
- This invention relates to a catalytic combustor that supplies di-fuel together with combustion air onto a catalyst body, causes an oxidation reaction to occur on the surface of the catalyst body, causes the catalyst body to generate heat, and utilizes the generated heat.
従来例の構成とその問題点
従来の触媒燃焼器の構成は、第1図に示した様に、円筒
状の燃焼筒A1内にハニカム形状をした円筒状の触媒体
A2、円板状の整流板A3を設置しただけのものであっ
た。この方式の場合、触媒体A2上で無炎燃焼を行わせ
た時、空気過剰率を小さくして行くと、もはや触媒体A
2上では無炎燃焼が行われずに、整流板A3上に火炎を
形成し、整流板A3が異常加熱し、整流板A3後方に丑
で火炎が移り危険となる欠点があった。したがって、こ
の構造では広範囲な空燃比での安定燃焼ができなかった
。Structure of the conventional example and its problems As shown in Fig. 1, the structure of the conventional catalytic combustor includes a honeycomb-shaped cylindrical catalyst body A2 in a cylindrical combustion cylinder A1, and a disk-shaped rectifier. It was just the installation of board A3. In this method, when flameless combustion is performed on the catalyst body A2, as the excess air ratio is decreased, the catalyst body A2 no longer burns.
2, flameless combustion did not occur and a flame was formed on the rectifying plate A3, which caused abnormal heating of the rectifying plate A3, and the flame was dangerously transferred to the rear of the rectifying plate A3. Therefore, with this structure, stable combustion could not be achieved over a wide range of air-fuel ratios.
また一方、火炎を併用する構造でも、第2図に示した様
に、触媒体B4の後方に炎孔板B6を設置しただけのも
のであり、火炎によって炎孔板B5が異常加熱を起こさ
せないためには、炎孔板B6の孔を小さくして噴出速度
を増大させ、火炎を3−
炎孔板B6から浮かせなければならなかった。したがっ
て火炎の状態が非常に不安定となり、特に空気過剰率を
大きくしていった場合触媒体B4の裏面に高温部、低温
部の分布ができ、低温部からCo等の未燃ガスが排出さ
れ、結果的に広い空燃比での安定燃焼ができなかった。On the other hand, even in a structure that uses flame, as shown in Figure 2, the flame hole plate B6 is simply installed behind the catalyst body B4, and the flame hole plate B5 is prevented from being abnormally heated by the flame. In order to achieve this, it was necessary to make the holes in the flame hole plate B6 smaller to increase the jet velocity and to float the flame from the flame hole plate B6. Therefore, the state of the flame becomes very unstable, and especially when the excess air ratio is increased, a high temperature area and a low temperature area are distributed on the back surface of the catalyst body B4, and unburned gas such as Co is discharged from the low temperature area. As a result, stable combustion over a wide range of air-fuel ratios was not possible.
発明の目的
本発明はかかる従来の間開を解消するもので、広範囲な
空燃比のもとでも安定かつ効率の良い酸化反応をさせる
と共に、排気ガスがクリーンとなる様な触媒燃焼器を提
供することを目的とする。OBJECTS OF THE INVENTION The present invention solves the conventional gap, and provides a catalytic combustor that allows stable and efficient oxidation reaction even under a wide range of air-fuel ratios and produces clean exhaust gas. The purpose is to
発明の構成
この目的を達成するために、本発明では予混合気流の上
流側に、予混合気噴出のための噴出孔を多数設けた噴出
板を備え、下流側にノ・ニカム式炎孔板を前記噴出板に
接触する様に設置し、さらに下流側に空間を開けて触媒
体を設置したことを基本構成とする。本構成で、噴出板
の噴出孔から噴き出す予混合ガスは、ハニカム式炎孔板
のセルを通電することにより整流され、ハニカム式炎孔
板出口付近で安定した火炎を形成する。さらに安定した
火炎の輻射熱により触媒体が均一に加熱され、活性化温
度に到達する。Structure of the Invention In order to achieve this object, the present invention includes a jetting plate provided with a large number of jetting holes for spouting the premixed air on the upstream side of the premixed air flow, and a no-nicum type flame hole plate on the downstream side. The basic configuration is that the catalyst body is installed so as to be in contact with the ejection plate, and a catalyst body is installed with a space left on the downstream side. With this configuration, the premixed gas ejected from the ejection holes of the ejection plate is rectified by energizing the cells of the honeycomb flame hole plate to form a stable flame near the outlet of the honeycomb flame hole plate. Furthermore, the catalyst body is uniformly heated by the radiant heat of the stable flame, and reaches the activation temperature.
一方、火炎燃焼で完全に燃焼しきれなかった未燃ガスは
、活性化温度を保っている触媒体上でさらに酸化され、
クリーンな排ガスとして排出される。したがって、空気
過剰率を高くして噴出板から強く噴出させても、ハニカ
ム式炎孔板のセルを通過する間に整流され、安定した火
炎を形成するため、触媒体の裏面に高温部、低温部の分
布ができにくいので、結果的に広い燃焼範囲を得ること
が可能となった。On the other hand, unburned gas that has not been completely combusted by flame combustion is further oxidized on the catalyst body that maintains the activation temperature.
It is emitted as clean exhaust gas. Therefore, even if the excess air ratio is high and the jet is strongly ejected from the ejection plate, the flame is rectified while passing through the cells of the honeycomb flame hole plate and a stable flame is formed. As a result, it is possible to obtain a wide combustion range.
実施例の説明
本発明による触媒燃焼器の一実施例を第3図に示し、こ
れにより説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of a catalytic combustor according to the present invention is shown in FIG. 3 and will now be described.
シーズヒータ6を埋設した気化予混合筒7内には、金網
またはパンチングメタル製の抵抗板8が設置され、気化
予混合筒7後力には、中央に空気口9を有する固定板1
0が接合されている。一方、気化予混合筒7の前方には
、多数の噴出小孔1161−ジ
を有する噴出板12が気化予混合筒7と一体構造を成す
様に設置され、さらに耐熱性金属からなる円筒状の燃焼
筒C13が接合されて因る。燃焼筒C13内には、その
前方に向かって耐熱性セラミックからなるハニカム式炎
孔板14が噴出板12の前面に接する様に設置され、さ
らに前方には円筒状の触媒体C15が順次設置されてい
る。また、ハニカム式炎孔板14のすぐ前方側には、点
火プラグ16が燃焼筒C13を貫通した形で設置されて
いる。一方、気化予混合筒7内に臨んだシャフト17の
先端には、前方に向は径が大となる円型台形のコーン1
82回転板192周端に攪拌用小羽根を有する混合板2
0が順次固定されている。A resistance plate 8 made of wire mesh or punching metal is installed inside the vaporization premixing cylinder 7 in which the sheathed heater 6 is embedded, and a fixed plate 1 having an air port 9 in the center is installed behind the vaporization premixing cylinder 7.
0 is joined. On the other hand, in front of the vaporization premixing cylinder 7, an ejection plate 12 having a large number of small ejection holes 1161 is installed so as to form an integral structure with the vaporization premixing cylinder 7, and a cylindrical plate made of heat-resistant metal is installed. This is due to the fact that the combustion cylinder C13 is joined. Inside the combustion tube C13, a honeycomb flame hole plate 14 made of heat-resistant ceramic is installed toward the front so as to be in contact with the front surface of the ejection plate 12, and further forward, cylindrical catalyst bodies C15 are sequentially installed. ing. Further, immediately in front of the honeycomb flame hole plate 14, a spark plug 16 is installed so as to penetrate through the combustion tube C13. On the other hand, at the tip of the shaft 17 facing into the vaporization premixing cylinder 7, there is a circular trapezoidal cone 1 whose diameter increases toward the front.
82 rotating plate 192 mixing plate 2 having small stirring blades on the peripheral edge
0 is fixed in sequence.
また、給油管21の先端はコーン18側方に開口する様
に設置されている。Further, the tip of the oil supply pipe 21 is installed so as to open to the side of the cone 18.
次に上記構成による実施例の作用を説明する。Next, the operation of the embodiment with the above configuration will be explained.
シーズヒ〜り6に通電され、気化予混合筒7の側壁が所
定の温度に到達すると、ファン、電磁ポンプ(共に図示
せず)に通電され、空気および液体燃料の供給が開始さ
れる。液体燃料は給油管216 ページ
によって回転中のコーン18上に送られコーン18のテ
ーパに沿って回転板19に達すると、その回転力により
円周方向に微粒子として飛赦し、定温状態の気化予混合
筒7の側壁に衝突し、直ちに気化する。一方、ファンに
よって取り込1れた空気は、空気口9から気化予混合筒
7内に送入され、混合板20により気化した液体燃料と
均一に混合され予混合ガスとなる。予混合ガスは抵抗板
8゜噴出板12.ハニカム式炎孔板14を通過したとこ
ろで、通電によりスパークを発している点火プラグ16
で点火される。点火によって生じた火炎は、予混合ガス
がハニカム式炎孔板14のセル内を通過することによっ
て整流されるため、安定な状態を保つ。この状態で火炎
からの輻射熱、燃焼筒C13からの伝熱を受けて触媒体
016が活性化温度に到達する。この時点で火炎燃焼に
より完全に燃焼しきれなかった予混合ガスは、活性化温
度を保っている触媒体C15上で完全に酸化され、クリ
ーンな排ガスとして排出される。また、空気過剰率を高
くしてもハニカム式炎孔板14のセル7ノパ
内で整流作用を受けるため、火炎は・・ニカム式炎孔板
14のすぐ上方に保炎され、安定な燃焼状態を保つ。し
たがって、触媒体C15の裏面には高温部、低温部の極
端な分布は起こらず、均一な温度状態を保つため、安定
な酸化状態を保つ。When the sheath heater 6 is energized and the side wall of the vaporization premix cylinder 7 reaches a predetermined temperature, the fan and electromagnetic pump (both not shown) are energized and the supply of air and liquid fuel is started. The liquid fuel is sent onto the rotating cone 18 through the fuel supply pipe 216, and when it reaches the rotating plate 19 along the taper of the cone 18, it is dispersed as fine particles in the circumferential direction by the rotational force, and is vaporized and premixed at a constant temperature. It collides with the side wall of cylinder 7 and immediately vaporizes. On the other hand, the air taken in by the fan is sent into the vaporization premix cylinder 7 through the air port 9, and is uniformly mixed with vaporized liquid fuel by the mixing plate 20 to become a premix gas. The premixed gas is passed through the resistance plate 8° and the ejection plate 12. After passing through the honeycomb flame hole plate 14, the spark plug 16 emits a spark when energized.
is ignited. The flame generated by ignition is rectified by the premixed gas passing through the cells of the honeycomb flame hole plate 14, so that the flame remains stable. In this state, the catalyst body 016 reaches the activation temperature by receiving radiant heat from the flame and heat transfer from the combustion tube C13. At this point, the premixed gas that has not been completely combusted by flame combustion is completely oxidized on the catalyst C15, which maintains the activation temperature, and is discharged as clean exhaust gas. In addition, even if the excess air ratio is increased, the flame is stabilized immediately above the honeycomb flame hole plate 14 because it receives a rectifying effect within the cell 7 nopa of the honeycomb flame hole plate 14, resulting in a stable combustion state. keep it. Therefore, extreme distribution of high-temperature and low-temperature regions does not occur on the back surface of the catalyst body C15, and a uniform temperature state is maintained, thereby maintaining a stable oxidation state.
本発明の触媒燃焼器による効果を実証するデータとして
、従来例として第 図、本発明実施例として第3図に示
したものを用いた場合の燃焼特性の相違を第4図に示し
た。尚、触媒体B4.触媒体C16は共にZrO2を担
体とし、酸化触媒としてN1を数多担持したものを用い
、燃料は灯油を使用した。As data to demonstrate the effects of the catalytic combustor of the present invention, Fig. 4 shows the difference in combustion characteristics when using the conventional example shown in Fig. 3 and the inventive example shown in Fig. 3. In addition, the catalyst body B4. The catalyst C16 used ZrO2 as a carrier and supported a large amount of N1 as an oxidation catalyst, and kerosene was used as the fuel.
図中、燃焼上限、燃焼下限の定義は、各々空気過剰率を
低下、増大させていった場合に、排ガス中にCoの発生
が起こり始める限界のC○2濃度を示す・第4図の燃焼
特性図より、従来例の場合は、特に低燃焼量領域に於け
る燃焼下限が高い、すなわち、空気過剰率を高くした場
合に安定燃焼状態が得られないことを示している。一方
、本発明実施例の場合は、測定を行った全燃焼量範囲で
、従来例よりも幅広い燃焼範囲を有している。In the figure, the definitions of combustion upper limit and combustion lower limit indicate the limit C○2 concentration at which Co starts to occur in the exhaust gas when the excess air ratio is decreased and increased, respectively.・The combustion shown in Figure 4 The characteristic diagram shows that in the case of the conventional example, the combustion lower limit is particularly high in the low combustion amount region, that is, a stable combustion state cannot be obtained when the excess air ratio is increased. On the other hand, in the case of the example of the present invention, the combustion range is wider than that of the conventional example in the entire range of combustion amount measured.
発明の効果
以上のことから、本発明の触媒燃焼器によれば次の効果
が得られる。Effects of the Invention In view of the above, the catalytic combustor of the present invention provides the following effects.
(1)多数の噴出小孔を有する噴出板にハニカム式炎孔
板を接触させる構成としているので、噴出小孔から噴出
する予混合気は、ハニカム式炎孔板のセルを通過するこ
とにより整流され、ハニカム式炎孔板上で安定した火炎
を形成する。(1) Since the honeycomb flame hole plate is in contact with the jet plate having a large number of small jet holes, the premixed gas ejected from the jet holes is rectified by passing through the cells of the honeycomb flame hole plate. A stable flame is formed on the honeycomb flame hole plate.
(2)・・ニカム式炎孔板からの安定した火炎により、
触媒体裏面が均一に加熱されるので、空気過剰率を高く
した場合でも極端な高温部、低温部の分布は起こりに<
<、結果的に広範囲な空燃比のもとでも安定燃焼を行う
ことができる。(2)... Due to the stable flame from the Nikam flame hole plate,
Since the back surface of the catalyst body is heated uniformly, even if the excess air ratio is increased, there will be no distribution of extremely high temperature and low temperature areas.
As a result, stable combustion can be achieved even under a wide range of air-fuel ratios.
第1図は従来の無炎型触媒燃焼器の要部縦断面図、第2
図は従来の火炎併用型触媒燃焼器の縦断面図、第3図は
本発明による触媒燃焼器の一実施例の縦断面図、第4図
は従来例と本発明実施例とを使用した場合の燃焼特性の
比較図である。
91−二゛
11・・・・・噴出小孔、12・・・・・・噴出孔、1
4・・・・・・ハニカム式炎孔板、16・・・・・・触
媒体C6代理人の氏名 弁理士 中 尾 敏 男 ほか
1名綜 綜
第3図 第
4図Figure 1 is a vertical cross-sectional view of the main parts of a conventional flameless catalytic combustor;
The figure is a longitudinal sectional view of a conventional flame-combined catalytic combustor, FIG. 3 is a longitudinal sectional view of an embodiment of a catalytic combustor according to the present invention, and FIG. 4 is a longitudinal sectional view of a conventional example and an embodiment of the present invention. FIG. 2 is a comparison diagram of the combustion characteristics of 91-2 11... small ejection hole, 12... ejection hole, 1
4...Honeycomb flame hole plate, 16...Catalyst body C6 Name of agent Patent attorney Toshio Nakao and one other person See Figure 3 Figure 4
Claims (3)
噴出させるための噴出孔を多数有した噴出板を備え、下
流側に火炎形成のための・・ニカム式炎孔板を前記噴出
板に接触する様に設置し、さらに下流側に空間を設けて
触媒体を設置した触媒燃焼器。(1) On the upstream side of the fuel-air premixed air flow, a blowout plate having a large number of blowholes for blowing out the premixed air is provided, and on the downstream side, a nicum type flame hole plate for forming a flame is provided as described above. A catalytic combustor is installed so that it is in contact with the ejection plate, and a space is provided on the downstream side where a catalyst body is installed.
も小さくした特許請求の範囲第1項記載の触媒燃焼器。(2) The catalytic combustor according to claim 1, wherein the porosity of the ejection plate is smaller than that of the honeycomb flame hole plate.
ミナ、ムライト、ムライト−ジルコン、ジルコニア等の
耐熱性セラミックを用いた特許請求の範囲第1項記載の
触媒燃焼器。(3) The catalytic combustor according to claim 1, wherein a heat-resistant ceramic such as alumina, mullite, mullite-zircon, or zirconia is used as the material of the carrier and the honeycomb flame hole plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2791483A JPS59153017A (en) | 1983-02-22 | 1983-02-22 | Catalytic burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2791483A JPS59153017A (en) | 1983-02-22 | 1983-02-22 | Catalytic burner |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59153017A true JPS59153017A (en) | 1984-08-31 |
Family
ID=12234145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2791483A Pending JPS59153017A (en) | 1983-02-22 | 1983-02-22 | Catalytic burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59153017A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0593121A1 (en) * | 1992-10-16 | 1994-04-20 | Process Combustion Corporation | Premix single stage low NOx burner |
US5326257A (en) * | 1992-10-21 | 1994-07-05 | Maxon Corporation | Gas-fired radiant burner |
US5711661A (en) * | 1994-05-03 | 1998-01-27 | Quantum Group, Inc. | High intensity, low NOx matrix burner |
US6213757B1 (en) | 1995-06-07 | 2001-04-10 | Quantum Group Inc. | Advanced emissive matrix combustion |
US6431857B1 (en) * | 1999-03-25 | 2002-08-13 | Sunkiss | Catalytic combustion device emitting infrared radiation |
US6632085B1 (en) * | 1999-08-19 | 2003-10-14 | Matsushita Electric Industrial Co., Ltd. | Catalyst combustion device and fuel vaporizing device |
-
1983
- 1983-02-22 JP JP2791483A patent/JPS59153017A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0593121A1 (en) * | 1992-10-16 | 1994-04-20 | Process Combustion Corporation | Premix single stage low NOx burner |
US5667374A (en) * | 1992-10-16 | 1997-09-16 | Process Combustion Corporation | Premix single stage low NOx burner |
US5326257A (en) * | 1992-10-21 | 1994-07-05 | Maxon Corporation | Gas-fired radiant burner |
US5711661A (en) * | 1994-05-03 | 1998-01-27 | Quantum Group, Inc. | High intensity, low NOx matrix burner |
US6213757B1 (en) | 1995-06-07 | 2001-04-10 | Quantum Group Inc. | Advanced emissive matrix combustion |
US6431857B1 (en) * | 1999-03-25 | 2002-08-13 | Sunkiss | Catalytic combustion device emitting infrared radiation |
US6632085B1 (en) * | 1999-08-19 | 2003-10-14 | Matsushita Electric Industrial Co., Ltd. | Catalyst combustion device and fuel vaporizing device |
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