JPH0221105A - Burner - Google Patents

Burner

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Publication number
JPH0221105A
JPH0221105A JP17042988A JP17042988A JPH0221105A JP H0221105 A JPH0221105 A JP H0221105A JP 17042988 A JP17042988 A JP 17042988A JP 17042988 A JP17042988 A JP 17042988A JP H0221105 A JPH0221105 A JP H0221105A
Authority
JP
Japan
Prior art keywords
fuel
flow passage
combustion gas
inlet
honeycomb
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.)
Granted
Application number
JP17042988A
Other languages
Japanese (ja)
Other versions
JP2681802B2 (en
Inventor
Saburo Maruko
三郎 丸子
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.)
Nippon Chemical Plant Consultant Co Ltd
Original Assignee
Nippon Chemical Plant Consultant 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
Priority to JP63170429A priority Critical patent/JP2681802B2/en
Application filed by Nippon Chemical Plant Consultant Co Ltd filed Critical Nippon Chemical Plant Consultant Co Ltd
Priority to DE1989609851 priority patent/DE68909851T2/en
Priority to EP92105621A priority patent/EP0493376B1/en
Priority to EP89112363A priority patent/EP0350032B1/en
Priority to DE1989624539 priority patent/DE68924539T2/en
Publication of JPH0221105A publication Critical patent/JPH0221105A/en
Priority to US07/814,226 priority patent/US5203690A/en
Priority to US07/850,649 priority patent/US5232358A/en
Application granted granted Critical
Publication of JP2681802B2 publication Critical patent/JP2681802B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Combustion Of Fluid Fuel (AREA)

Abstract

PURPOSE:To obtain combustion gas which is free of NOX and unburnt substances by laying out a return flow passage within a forward flow passage so that they may be connected with each other in a folding manner separated by a cylinder-shaped wall, and installing a main stream inlet which is adapted to connect a fuel mixer with the upper stream side of said forward flow passage and auxiliary stream inlet which connects a pilot burner to said forward flow passage, and connecting the outlet of combustion gas with the downstream side of said forward flow passage. CONSTITUTION:Combustion gas is adapted to flow into a forward flow passage 3 of a burner from an auxiliary flow inlet 6 by operating a pilot burner 12 so as to heat an outer cylinder 1 and an inner cylinder 2 on the upper stream side. At the time when this portion is heated to about 900 deg.C and over, a fuel mixer 11 is made to operate so that fuel mixed air may flow to the upper stream side of the forward passage 3. At that time, the pilot burner 12 is adapted to come to a halt. The fuel mixed gas which has flown into the upper stream side from the fuel mixer 11 by way of a main stream inlet 5 under this condition is brought into contact with the side walls of the outer cylinder and the inner cylinder on the upper stream side of the heated forward flow passage and starts combustion. The combustion gas is discharged from an outlet 7, passing through a return flow passage 4 from the forward flow passage 3. Therefore, the fuel contained in the fuel mixed gas which has been introduced from the fuel mixer 11 can be burnt to a satisfactory extent until it has reached the outlet of the return flow passage 4.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、高温の燃焼ガスを得るための燃焼器に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a combustor for obtaining high-temperature combustion gas.

〔従来の技術〕[Conventional technology]

上記燃焼器で得られる燃焼ガスは、公害物質、すなわち
NOx及び未燃物がなく、かつ完全燃焼して残留02が
低いことが望ましい。
It is desirable that the combustion gas obtained in the combustor be free of pollutants, ie, NOx and unburned materials, and be completely combusted and have a low residual O2 content.

従来のこの種の燃焼器にあっては、(1)空気と燃料を
爆発限界範囲内の濃度で混合し、これを電気のスパーク
等の手段にて着火させて火炎の形成をなし、その後は上
記空気と燃料の混合ガスを継続して燃焼させるようにし
た燃焼器、(2)予熱された空気中に燃料を混合して燃
焼触媒により燃焼させるようにした燃焼器、(3)本願
発明者が先に特開昭62〜11[1808号公報で提案
したように、主燃焼器の加熱管の外側を補助燃焼器にて
常時燃料の着火温度以上に加熱し、主燃焼器では上記加
熱された加熱管に燃料を接触させて燃焼を継続させるよ
うにした燃焼器がそれぞれ知られている。
In conventional combustors of this type, (1) air and fuel are mixed at a concentration within the explosion limit, ignited by means such as an electric spark to form a flame; A combustor configured to continuously burn the above-mentioned mixed gas of air and fuel, (2) a combustor configured to mix fuel into preheated air and combust it using a combustion catalyst, (3) the inventor of the present application As previously proposed in Japanese Unexamined Patent Publication No. 1808/1983, the outside of the heating tube of the main combustor is constantly heated above the ignition temperature of the fuel in the auxiliary combustor, and the above-mentioned heating is performed in the main combustor. There are known combustors that continue combustion by bringing fuel into contact with heated tubes.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来の燃焼器のうち、(1)のものにあっては、火
炎を形成するために部分的に高温の部分が存在し、その
ためにNOxの発生が避けられなかった。また空気と燃
料の混合及び燃焼は極めて短かい時間内で行なわれるた
め、燃焼ガス中に未燃物や残留02が多い等問題がある
Among the above-mentioned conventional combustors, the one in (1) has a partially high-temperature portion to form a flame, and therefore the generation of NOx is unavoidable. Furthermore, since the mixing and combustion of air and fuel are carried out within an extremely short period of time, there are problems such as a large amount of unburned matter and residual O2 in the combustion gas.

また上記(2)のものにあっては、低温での燃焼が可能
であるが、燃焼温度が1300℃以上になると燃焼触媒
の寿命が短<、長期の運転は不可能であり、また燃焼触
媒の場合、触媒毒となる硫黄分を含有する燃料を使用す
ることができない。
In addition, in the case of (2) above, combustion is possible at low temperatures, but if the combustion temperature exceeds 1300°C, the life of the combustion catalyst is short, and long-term operation is impossible, and the combustion catalyst In this case, fuel containing sulfur, which poisons the catalyst, cannot be used.

さらに上記(3)のものにあっては、主燃焼器のほかに
、補助燃焼器を常時燃焼させておかなければならないた
め、燃焼の制御を主燃焼器と補助燃焼器の双方について
行なわなければならずやっかいであった。またこの従来
例のものにあっても燃焼ガス中のNOxを完全になくす
ことはできなかった。
Furthermore, in the case of (3) above, in addition to the main combustor, the auxiliary combustor must be kept burning at all times, so combustion control must be performed for both the main combustor and the auxiliary combustor. It was rather troublesome. Further, even with this conventional example, NOx in the combustion gas could not be completely eliminated.

本発明は上記のことにかんがみなされたもので、公害物
質であるN Ox及び未燃物がない燃焼ガスを得ること
ができるようにした燃焼器を提供することを目的とする
ものである。
The present invention was conceived in view of the above, and an object of the present invention is to provide a combustor that can obtain combustion gas free of pollutant NOx and unburned substances.

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

上記目的を達成するために、本発明に係る燃焼器は、筒
状の往側流路内に復側流路を筒状の壁を隔てて折り返し
状に接続して配置し、上記往側流路の上流側に燃料混合
器を接続した主流入口と、パイロットバーナを接続した
補助流入口とを設け、復側流路の下流側を燃焼ガスの出
口を接続した構成となっている。
In order to achieve the above object, the combustor according to the present invention has a cylindrical outgoing flow path and a return side flow path connected in a folded manner across a cylindrical wall. A main inlet connected to a fuel mixer and an auxiliary inlet connected to a pilot burner are provided on the upstream side of the flow path, and a combustion gas outlet is connected to the downstream side of the return flow path.

また断面形状を円筒状にした枠筒内に、円筒状で、かつ
通路を軸方向に設けたハニカム状通路を回転可能に設け
、また上記枠筒内の軸方向一側部に、仕切壁にて直径方
向に仕切られた流入室と流出室を、また他側部に燃焼ガ
ス室をそれぞれハニカム状通路の軸方向端面に対向させ
て設け、上記流入室に燃料混合ガス流入口とパイロット
バーナを、また流出室に燃焼ガスの出口をそれぞれ設け
、上記ハニカム状通路の支軸を回転装置に接続した構成
となっている。
In addition, a honeycomb-shaped passage having a cylindrical shape and a passage in the axial direction is rotatably provided in the frame cylinder having a cylindrical cross-sectional shape, and a partition wall is provided on one side in the axial direction of the frame cylinder. An inflow chamber and an outflow chamber partitioned in the diametrical direction are provided on the other side, and a combustion gas chamber is provided on the other side facing the axial end surface of the honeycomb-shaped passage, and a fuel mixed gas inlet and a pilot burner are provided in the inflow chamber. Further, the outflow chambers are each provided with an outlet for combustion gas, and the supporting shaft of the honeycomb-shaped passage is connected to a rotating device.

さらに上記ハニカム状通路の通路壁面に燃焼触媒を担持
させてもよい。
Furthermore, a combustion catalyst may be supported on the wall surface of the honeycomb-shaped passage.

〔作 用〕[For production]

往側流路の上流側の壁面をパイロットバーナからの燃焼
ガスにて90℃以上に加熱してから燃料混合ガスを主流
入口より往側流路の上流側に流入させる。この燃料混合
ガスは加熱された壁面に接触して燃焼され、この燃焼ガ
スは往側流路から復側流路を折り返し流れて出口へ流出
され、往側流路と復側流路を隔てる壁は両流路に面した
両側から加熱される。上記パイロットバーナは往側流路
の上流側が所定の温度に加熱される間にわたってのみ運
転する。
The upstream wall surface of the outgoing flow path is heated to 90° C. or higher with combustion gas from the pilot burner, and then the fuel mixture gas is allowed to flow into the upstream side of the outgoing flow path from the main stream inlet. This fuel mixture gas comes into contact with the heated wall surface and is combusted, and this combustion gas flows back from the outgoing flow path through the return flow path and flows out to the outlet, and is then combusted by the wall that separates the outbound flow path and the return flow path. is heated from both sides facing both channels. The pilot burner operates only while the upstream side of the outgoing flow path is heated to a predetermined temperature.

また外筒内でハニカム状通路を回転させるようにした燃
焼器にあっては、ハニカム状通路を回転させることによ
り、燃焼ガスで加熱されたハニカム状通路の側面に順次
流入室に流入した燃料混合ガスが接触してこれが燃焼さ
れる。ハニカム状通路は流入室から流入した燃料混合ガ
スの燃焼と燃焼ガス室から流出室へ流れる燃焼ガスにて
加熱され、燃焼ガス室からの燃焼ガスにて加熱された部
分が回転に従って順次流入室に対向される。
In addition, in a combustor in which a honeycomb-shaped passage is rotated within the outer cylinder, by rotating the honeycomb-shaped passage, the fuel mixture that is heated by the combustion gas and sequentially flows into the inlet chamber is heated on the side of the honeycomb-shaped passage. The gases come into contact and are combusted. The honeycomb-shaped passage is heated by the combustion of the fuel mixture gas that flows in from the inflow chamber and the combustion gas flowing from the combustion gas chamber to the outflow chamber, and the portion heated by the combustion gas from the combustion gas chamber sequentially flows into the inflow chamber as it rotates. faced.

上記ハニカム状通路の壁面に燃焼触媒を担持することに
より、燃料混合ガスはこの燃焼触媒に接触して燃焼され
、予熱温度が低い燃料混合ガスでも燃焼される。
By supporting a combustion catalyst on the wall surface of the honeycomb-shaped passage, the fuel mixture gas comes into contact with the combustion catalyst and is combusted, and even the fuel mixture gas whose preheating temperature is low is combusted.

〔実 施 例〕 本発明の実施例を図面に基づいて説明する。〔Example〕 Embodiments of the present invention will be described based on the drawings.

第1図、第2図は本発明の第1の実施例を示すもので、
図中1は外筒、2はこの外筒1の内側に略同心状にして
配置された内筒であり、これらはセラミックスにて構成
されている。そしてこの両筒1,2にてリング状の往側
流路3と、この往側流路3内に配置される円筒状の復側
流路4が構成され、往側流路3の上流端は閉じられ、下
流端は復側流路4の上流端に、外筒1の端部で構成され
る空間にて折り返し状に連通されている。そして上記往
側流路3の上流端部の側壁に主流入口5と、補助流入口
6とが開口されており、また復側流路4の下流端部は出
口7に開口されている。また上記往側流路3の下流端部
と復側流路4の下流端部にはそれぞれドーナツ状、栓状
に形成したセラミックス製の・にカム状流路8.9が介
装されている。
1 and 2 show a first embodiment of the present invention,
In the figure, 1 is an outer cylinder, and 2 is an inner cylinder arranged approximately concentrically inside the outer cylinder 1, and these are made of ceramics. The two cylinders 1 and 2 constitute a ring-shaped outgoing flow path 3 and a cylindrical return flow path 4 disposed within the outgoing flow path 3, and the upstream end of the outgoing flow path 3 is closed, and its downstream end communicates with the upstream end of the return flow path 4 in a folded manner in a space formed by the end of the outer cylinder 1. A main stream inlet 5 and an auxiliary inlet 6 are opened in the side wall at the upstream end of the outgoing flow path 3, and an outlet 7 is opened at the downstream end of the return flow path 4. Further, a cam-shaped flow path 8.9 made of ceramics and formed in a donut shape and a plug shape is interposed at the downstream end of the outgoing flow path 3 and the downstream end of the return flow path 4, respectively. .

上記外筒1は断熱材10を介して外枠10aに支持さて
いる。
The outer cylinder 1 is supported by an outer frame 10a via a heat insulating material 10.

上記往側流路3の上流側に設けられた主流入日5には燃
料混合器11が、また補助流入口6にはパイロットバー
ナ12がそれぞれ接続されている。そして上記主燃料混
合器11には予熱空気流入管13と、燃料流入管14と
が接続されており両流入管13.14から流入された空
気と燃料は空気−燃料混合部15にて混合されて燃料混
合ガスとして往側流路3の上流側へ流入されるようにな
っている。またパイロットバーナ12は空気流入管16
と燃料流入管17が接続されていて、このパイロットバ
ーナ12の燃料ガスは往側流路3の上流側へ流入される
ようになっている。
A fuel mixer 11 is connected to the main inlet 5 provided on the upstream side of the outgoing flow path 3, and a pilot burner 12 is connected to the auxiliary inlet 6. A preheated air inflow pipe 13 and a fuel inflow pipe 14 are connected to the main fuel mixer 11, and the air and fuel flowing in from both inflow pipes 13 and 14 are mixed in an air-fuel mixing section 15. The mixed gas is then flowed into the upstream side of the outgoing flow path 3 as a fuel mixed gas. The pilot burner 12 also has an air inlet pipe 16.
A fuel inlet pipe 17 is connected to the pilot burner 12 so that the fuel gas from the pilot burner 12 is allowed to flow into the upstream side of the outgoing flow path 3.

上記構成において、まずパイロットバーナ12を運転し
てこれからの燃焼ガスを燃焼器の往側流路3内に流入さ
せてこの往側流路3の上流側の外筒1と内筒2を加熱す
る。そしてこの部分が約900℃以上に加熱された時点
で燃料混合器11を作動させて往側流路3の上流側へ燃
料混合空気を流入させる。このとき、上記パイロットバ
ーナ12は直ちに、あるいは多少オーバラップして停止
させる。
In the above configuration, first, the pilot burner 12 is operated to cause future combustion gas to flow into the outgoing flow path 3 of the combustor, thereby heating the outer cylinder 1 and the inner cylinder 2 on the upstream side of the outgoing flow path 3. . When this portion is heated to about 900° C. or higher, the fuel mixer 11 is operated to cause the fuel mixed air to flow into the upstream side of the outgoing flow path 3. At this time, the pilot burner 12 is stopped immediately or with some overlap.

上記状態で、燃料混合器11より主流入口5を介して流
入した燃料混合ガスは往側流路3の加熱された上流側の
外筒1、内筒2の側壁に接触して燃焼を開始し、その燃
焼ガスは往側流路3から復側流路4を通って出口7より
排出され、この間に上記両流路3,4の各側壁は順次加
熱されてゆき、これにより、上記燃料混合器11より流
入した燃料混合ガス中の燃料は順次燃焼して復側流路4
の出口に達するまでに完全に燃焼される。この場合、燃
料混合器11での燃料は燃焼ガスの温度が1200〜1
400℃になるように予熱した空気中に混合する。
In the above state, the fuel mixture gas flowing from the fuel mixer 11 through the main stream inlet 5 contacts the heated side walls of the outer cylinder 1 and inner cylinder 2 on the upstream side of the outgoing flow path 3 and starts combustion. The combustion gas passes from the outgoing flow path 3 to the return flow path 4 and is discharged from the outlet 7. During this time, the side walls of both the flow paths 3 and 4 are sequentially heated, and as a result, the fuel mixture is heated. The fuel in the fuel mixture gas that has flowed in from the vessel 11 is sequentially combusted and flows into the return side flow path 4.
completely burnt out by the time it reaches the outlet. In this case, the fuel in the fuel mixer 11 has a combustion gas temperature of 1200 to 1
Mix in air preheated to 400°C.

上記燃焼作用時において、往側流路3の上流部で開始さ
れた燃焼は往側流路3から復側流路4を通る間にわたっ
て継続され、内筒2はこれの往側と復側の双方から加熱
される。また燃焼ガスは往側流路3の下流端と、復側流
路4の下流端にそれぞれ設けられたハニカム状流路8゜
9を通る間に完全燃焼される。またこのとき、外筒1の
内面に赤外線の吸収率の高い塗料を塗布しておくことに
より、内筒2の外面から放射される赤外線の吸収率が高
くなって外筒1の内面温度が高くなり、この外筒2の内
面も燃料混合ガスを燃焼させるための発熱面として利用
できる。
During the above-mentioned combustion operation, the combustion started at the upstream part of the outgoing flow path 3 continues from the outgoing flow path 3 to the return side flow path 4, and the inner cylinder 2 is Heated from both sides. Further, the combustion gas is completely combusted while passing through the honeycomb-shaped channels 8.9 provided at the downstream end of the outgoing channel 3 and the downstream end of the returning channel 4, respectively. Also, at this time, by applying a paint with a high absorption rate of infrared rays to the inner surface of the outer cylinder 1, the absorption rate of infrared rays emitted from the outer surface of the inner cylinder 2 becomes high, and the inner temperature of the outer cylinder 1 becomes high. Therefore, the inner surface of the outer cylinder 2 can also be used as a heat generating surface for burning the fuel mixture gas.

第3図から第5図は本発明の第2の実施例を示すもので
、上記第1の実施例と同じ構成部材は第1図、第2図に
示すものと同一符号を付して説明を省略する。
3 to 5 show a second embodiment of the present invention, and the same constituent members as in the first embodiment are designated by the same reference numerals as those shown in FIGS. 1 and 2. omitted.

セラミックス製の外筒21内に複数本のセラミックス製
の内筒22を配置してこの内筒22の周囲に往側流路2
3を構成し、内筒22の内側に復側流路24を構成する
。そして上記往側流路23の上流側は各内筒22の下流
側を支持する支壁25にて閉じられており、また往側流
路23の下流側及び復側流路24の下流側にはハニカム
状通路26.27が介装しである。また、上記往側通路
23内には、迷路用のバッフルプレート28が複数枚介
装しである。
A plurality of inner cylinders 22 made of ceramic are arranged inside an outer cylinder 21 made of ceramic, and an outgoing flow path 2 is formed around the inner cylinder 22.
3, and a return side flow path 24 is configured inside the inner cylinder 22. The upstream side of the outgoing flow path 23 is closed by a branch wall 25 that supports the downstream side of each inner cylinder 22, and the downstream side of the outgoing flow path 23 and the downstream side of the return side flow path 24 are closed. In this case, honeycomb-like passages 26 and 27 are interposed. Further, a plurality of baffle plates 28 for a maze are interposed in the outgoing passage 23.

この実施例は燃焼量が多い場合に有利であって、その燃
焼作用は上記第1の実施例と同じである。
This embodiment is advantageous when the amount of combustion is large, and its combustion action is the same as that of the first embodiment.

すなわち、まずパイロットバーナ12にて往側流路23
の上流側の流路壁を所定の温度(900℃)以上に加熱
してから燃料混合器11より燃料混合ガスを往側流路2
3内に流入させて燃焼させる。このとき、往側流路23
内での燃焼ガスはバッフルプレート28にて構成される
迷路を通ってこれの下流端に流れ、この間に燃料混合ガ
スは充分撹拌されて燃焼される。往側流路23の下流体
に流れた燃焼ガスはハニカム状通路26を経て復側流路
24に入り、この復側流路24を構成する加熱された内
筒22の内壁温度でさらに燃焼が促進されてこれの下流
側のハニカム状通路27を経て出口7より排出される。
That is, first, the pilot burner 12 burns the outgoing flow path 23.
After heating the flow passage wall on the upstream side of the
3 and burn it. At this time, the outgoing flow path 23
The combustion gas within flows to the downstream end of the labyrinth formed by the baffle plate 28, during which time the fuel mixture gas is sufficiently stirred and combusted. The combustion gas that has flowed into the lower fluid of the outgoing flow path 23 enters the return flow path 24 through the honeycomb-shaped passage 26, and is further combusted at the temperature of the inner wall of the heated inner cylinder 22 that constitutes the return flow path 24. It is accelerated and discharged from the outlet 7 through the honeycomb-shaped passage 27 on the downstream side.

第6図、第7図は本発明の第3の実施例を示すもので、
図中31は軸芯を上下方向に向けて円筒状に構成された
セラミックス製の枠筒であり、この枠筒31内の中間部
にセラミックにて+M成されたハニカム状通路32が同
軸心上に回転自在に嵌合されている。モして枠筒31の
上部で、かつハニカム状通路32の上方に対向する位置
に、仕切壁33にて左右方向に仕切られたが人口室34
aと、出口室34bとが設けられている。上記入口室3
4aに燃料混合ガスの流入口35が、また出口室34b
に燃焼ガスの流出口36が開口されている。また枠筒3
1の下部で、かつハニカム状通路32の下方に対向する
位置に燃焼ガス室37が設けられている。
6 and 7 show a third embodiment of the present invention,
In the figure, reference numeral 31 denotes a ceramic frame tube configured in a cylindrical shape with its axis directed in the vertical direction, and a honeycomb-shaped passage 32 made of ceramic and made of +M is coaxially located in the middle part of this frame tube 31. It is rotatably fitted to the A population chamber 34 is partitioned in the left and right direction by a partition wall 33 at the upper part of the frame cylinder 31 and at a position facing above the honeycomb-like passage 32.
a and an outlet chamber 34b. Above entrance room 3
4a has an inlet 35 for the fuel mixture gas, and an outlet chamber 34b
A combustion gas outlet 36 is opened in the opening. Also frame tube 3
A combustion gas chamber 37 is provided at the lower part of the honeycomb passageway 1 and at a position facing below the honeycomb-like passage 32 .

上記ハニカム状通路32の軸心に支軸38が設けてあり
、この支軸38の下端部が支枠39に支承されていると
共に回転装置40に連結さている。ハニカム状通路32
の全ての断面位置においてハニカム壁で仕切られた細か
い通路が軸方向に構成されており、各通路の上端は入口
室34aあるいは出口室34bに開口され、下端は燃焼
ガス室37に開口されている。
A support shaft 38 is provided at the axial center of the honeycomb-shaped passage 32, and the lower end of this support shaft 38 is supported by a support frame 39 and connected to a rotating device 40. Honeycomb-like passage 32
Fine passages partitioned by honeycomb walls are formed in the axial direction at all cross-sectional positions, and the upper end of each passage opens into the inlet chamber 34a or the outlet chamber 34b, and the lower end opens into the combustion gas chamber 37. .

上記入口室34aには流入口35のほかに、第1図に示
すものと同様のパイロットバーナ12が接続されている
。また枠筒31は断熱材41にて囲繞されている。
In addition to the inlet port 35, a pilot burner 12 similar to that shown in FIG. 1 is connected to the inlet chamber 34a. Further, the frame tube 31 is surrounded by a heat insulating material 41.

上記構成において、ハニカム状通路32は常時所定の回
転速度で回転させておく。この状態でまずスタート用の
パイロットバーナ12よりの燃焼ガスを人口室34a内
に流入させる。この燃焼ガスにより入口室34a及びハ
ニカム状通路32の上流側が加熱される。このときハニ
カム状通路32は回転しているので、ハニカム状通路3
2の上端部全体が順次入口室34aにて加熱される。こ
の部分が所定の温度(900℃)になった状態で上記パ
イロットバーナ12からの加熱を停止して流入口35よ
り予熱された燃料混合ガスを流入させる。燃料混合ガス
は入口室34aよりハニカム状通路32に至る往側流路
にて加熱された壁面に接触することにより燃焼を開始し
、この往側流路にて燃焼ガス室37までで燃焼が終了す
る。燃焼ガス室37の燃焼ガスは、ハニカム状通路32
の出口室34bに対向している部分の通路である復側流
路を通って出口室34bに至り、ここから流出口36へ
流出される。このとき、ハニカム状通路32の出口室3
4bに対向している復側流路は、上記燃焼ガス室37か
らの燃焼ガスによって加熱され、この部分がハニカム状
通路32の回転により順次人口室34aに対向する往側
流路側の位置に移動する。従って入口室34aに流入し
た燃料混合はハニカム状通路32の加熱された往側流路
の壁面に順次接触してこれの燃焼が継続される。
In the above configuration, the honeycomb passage 32 is always rotated at a predetermined rotational speed. In this state, first, the combustion gas from the pilot burner 12 for starting is allowed to flow into the artificial chamber 34a. This combustion gas heats the inlet chamber 34a and the upstream side of the honeycomb passage 32. At this time, since the honeycomb-shaped passage 32 is rotating, the honeycomb-shaped passage 32
The entire upper end of the tube 2 is sequentially heated in the inlet chamber 34a. When this portion reaches a predetermined temperature (900° C.), heating from the pilot burner 12 is stopped and preheated fuel mixture gas is allowed to flow in from the inlet 35. The fuel mixture gas starts combustion by contacting the heated wall surface in the outgoing flow path from the inlet chamber 34a to the honeycomb-shaped passage 32, and combustion ends in this outgoing flow path up to the combustion gas chamber 37. do. The combustion gas in the combustion gas chamber 37 flows through the honeycomb-shaped passage 32.
It reaches the outlet chamber 34b through the return side flow path, which is a passageway in the portion facing the outlet chamber 34b, and flows out from there to the outlet 36. At this time, the outlet chamber 3 of the honeycomb-like passage 32
4b is heated by the combustion gas from the combustion gas chamber 37, and this portion is sequentially moved to a position on the outgoing flow path side facing the population chamber 34a by the rotation of the honeycomb-shaped passage 32. do. Therefore, the fuel mixture that has flowed into the inlet chamber 34a sequentially comes into contact with the heated wall surface of the outgoing channel of the honeycomb-shaped passage 32, and its combustion continues.

さらに第4の実施例として、上記第3の実施例において
、第6図、第7図にて示した回転するハニカム状通路3
2の各壁面に燃焼触媒を担持させる。この燃焼触媒は白
金、パラジウム等からなるもので、これの上記各壁面へ
の付着は、溶解した上記燃焼触媒中にハニカム状通路3
2を浸漬することにより行なう。
Furthermore, as a fourth embodiment, in the third embodiment, the rotating honeycomb-shaped passage 3 shown in FIGS.
A combustion catalyst is supported on each wall surface of No. 2. This combustion catalyst is made of platinum, palladium, etc., and its adhesion to the above-mentioned walls is caused by the formation of honeycomb-shaped passages in the melted combustion catalyst.
This is done by dipping 2.

この実施例によれば、パイロットバーナ12による壁面
の加熱温度が900℃以下でも壁面燃焼が可能になる。
According to this embodiment, wall combustion is possible even when the heating temperature of the wall surface by the pilot burner 12 is 900° C. or lower.

すなわち、予熱空気中に燃料を混合して燃料混合ガスを
作るのであるが、燃料がガス体の場合は予熱なしで、ま
た燃料が液体の場合には空気中における燃料の分圧が露
点よりも少し高い温度までの予熱でよく、空気の予熱温
度を極端に低くすることが可能である。
In other words, a fuel mixture gas is created by mixing fuel in preheated air, but if the fuel is a gas, no preheating is required, or if the fuel is a liquid, the partial pressure of the fuel in the air is lower than the dew point. Preheating to a slightly higher temperature is sufficient, and it is possible to preheat the air to an extremely low temperature.

なおこの実施例の場合には、燃料中に硫黄分等の触媒毒
が存在しているものは使用できない。
In this embodiment, fuel containing catalyst poisons such as sulfur cannot be used.

上記各実施例における外筒1,21及び内筒2.22、
枠筒31さらにハニカム状通路8゜9.26,27.3
2を構成するセラミックスの材質は強度、耐熱温度、さ
らに耐熱衝撃の点で優れている炭化硅素が用いられる。
The outer cylinders 1 and 21 and the inner cylinders 2 and 22 in each of the above embodiments,
Frame cylinder 31 and honeycomb-like passage 8°9.26, 27.3
Silicon carbide, which is excellent in strength, temperature resistance, and thermal shock resistance, is used as the material for the ceramic component 2.

しかしこれに限定されるものではなく、ジルコニア系、
コージライト系のセラミックスでもよい。
However, it is not limited to this, and includes zirconia,
Cordierite-based ceramics may also be used.

また外筒1,21及び枠筒31はアルミナ繊維を主成分
とするもので成形したものを使用してもよい。この場合
には筒の内面に赤外線の吸収率の高い5iZr04また
はMnO2・Cr2O3等の酸化物を主体とする塗料を
スプレ等の手段にて密着するのが望ましい。
Further, the outer cylinders 1, 21 and the frame cylinder 31 may be molded from materials whose main component is alumina fiber. In this case, it is desirable to apply a coating material mainly composed of 5iZr04 or an oxide such as MnO2.Cr2O3, which has a high infrared absorption rate, to the inner surface of the cylinder by means such as spraying.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、往側流路3,23から復側流路4,2
4へ折り返し流れる燃焼ガスによって、両通路を隔てる
壁は、これの両側から、往側流路3,23の上流側に流
入される燃料混合ガスが接触して燃焼するに充分な温度
に加熱され、両通路を通る間に完全に燃焼されて復側流
路4.24の下流側に設けた出口7からは、公害物質で
あるNOX及び未燃物がなく、また燃焼器を多段にシリ
ーズに接続して使用することにより、燃焼は完全燃焼に
より残留02が極端に低い燃焼ガスを得ることができる
According to the present invention, from the outgoing channels 3, 23 to the returning channels 4, 2
4, the wall separating both passages is heated to a temperature sufficient for the fuel mixture gas flowing into the upstream side of the outgoing passages 3 and 23 from both sides to contact and burn. , the combustion is completed while passing through both passages, and there is no pollutant NOx and unburned substances from the outlet 7 provided on the downstream side of the return flow passage 4.24, and the combustor is arranged in series in multiple stages. By connecting and using them, it is possible to obtain combustion gas with extremely low residual O2 through complete combustion.

また燃焼ガスの通路となるハニカム状通路32が燃焼ガ
スの往側流路−復側流路にわたって回転されることによ
り、復側流路にて加熱された部分が順次往側流路側に移
動され、往側流路に流入した燃料混合ガスは上記流路の
壁面により良好な状態で継続燃焼される。
In addition, by rotating the honeycomb-shaped passage 32, which serves as a passage for combustion gas, between the outgoing and returning passages of the combustion gas, the portion heated in the returning passage is sequentially moved to the outgoing passage. The fuel mixture gas that has flowed into the outgoing flow path is continuously combusted in a good condition by the wall surface of the flow path.

さらに上記ハニカム状通路の壁面に燃焼触媒を担持した
ことにより、予熱温度が低い燃料混合ガスでも良好に燃
焼される。
Furthermore, since a combustion catalyst is supported on the wall surface of the honeycomb-shaped passage, even a fuel mixture gas whose preheating temperature is low can be burned satisfactorily.

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

第1図は本発明の第1の実施例を示す断面図、第2図は
第1図の■−■線に沿う断面矢視図、第3図は本発明の
第2の実施例を示す断面図、第4図は第3図のIV−I
V線に沿う断面矢視図、第5図は第3図v−v線に沿う
断面矢視図、第6図は本発明の第3の実施例を示す断面
図、第7図は第6図の■−■線に沿う断面矢視図である
。 3.23は往側流路、4,24は復側流路、5は主流入
口、6は補助流入口、7は出口、11は燃料混合器、1
2はパイロットバーナ、31は枠筒、32はハニカム状
通路、33は仕切壁、34aは流入室、34bは流出室
、35は燃料混合ガス流入口、37は燃焼ガス室、38
は支軸、40は回転装置。 第 図
FIG. 1 is a cross-sectional view showing a first embodiment of the present invention, FIG. 2 is a cross-sectional view taken along the line ■-■ in FIG. 1, and FIG. 3 is a cross-sectional view showing a second embodiment of the present invention. Cross-sectional view, Figure 4 is IV-I in Figure 3.
5 is a sectional view taken along line V--V in FIG. 3, FIG. 6 is a sectional view showing the third embodiment of the present invention, and FIG. It is a cross-sectional view taken along the line ■-■ in the figure. 3.23 is the outgoing flow path, 4 and 24 are the return side flow paths, 5 is the main inlet, 6 is the auxiliary inlet, 7 is the outlet, 11 is the fuel mixer, 1
2 is a pilot burner, 31 is a frame cylinder, 32 is a honeycomb-shaped passage, 33 is a partition wall, 34a is an inlet chamber, 34b is an outlet chamber, 35 is a fuel mixed gas inlet, 37 is a combustion gas chamber, 38
is a support shaft, and 40 is a rotating device. Diagram

Claims (3)

【特許請求の範囲】[Claims] (1)筒状の往側流路3、23内に、復側流路4、24
を筒状の壁を隔てて折り返し状に接続して配置し、上記
往側流路4、24の上流側に燃料混合器11を接続した
主流入口5と、パイロットバーナ12を接続した補助流
入口6を設け、復側流路4、24の下流端を出口7に接
続したことを特徴とする燃焼器。
(1) Inside the cylindrical outgoing channels 3, 23, the returning channels 4, 24
are connected in a folded manner across a cylindrical wall, and the main inlet 5 is connected to the fuel mixer 11 on the upstream side of the outgoing channels 4 and 24, and the auxiliary inlet is connected to the pilot burner 12. 6, and the downstream ends of the return side flow paths 4 and 24 are connected to the outlet 7.
(2)断面形状を円筒状にした枠筒31内に、円筒状で
、かつ通路を軸方向に設けたハニカム状通路32を回転
可能に設け、また上記枠筒31内の軸方向一側部に、仕
切壁33にて直径方向に仕切られた流入室34aと流出
室34bを、また他側部に燃焼ガス室37をそれぞれ上
記ハニカム状通路32の軸方向端面に対向させて設け、
上記流入室34aに燃料混合ガス流入口35とパイロッ
トバーナ12を、また流出室34bに燃焼ガスの流出口
36をそれぞれ設け、上記ハニカム状通路32の支軸3
8を回転装置40に接続したことを特徴とする燃焼器。
(2) A honeycomb-shaped passage 32 which is cylindrical and has a passage in the axial direction is rotatably provided in the frame tube 31 having a cylindrical cross-sectional shape, and one side of the frame tube 31 in the axial direction An inflow chamber 34a and an outflow chamber 34b diametrically partitioned by a partition wall 33 are provided, and a combustion gas chamber 37 is provided on the other side facing the axial end surface of the honeycomb-shaped passage 32, respectively.
The inlet chamber 34a is provided with a fuel mixed gas inlet 35 and the pilot burner 12, and the outlet chamber 34b is provided with a combustion gas outlet 36.
8 is connected to a rotating device 40.
(3)ハニカム状通路32の通路壁面に燃焼触媒を担持
させたことを特徴とする請求項2記載の燃焼器。
(3) The combustor according to claim 2, wherein a combustion catalyst is supported on the wall surface of the honeycomb-shaped passage 32.
JP63170429A 1988-07-08 1988-07-08 Combustor Expired - Lifetime JP2681802B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP63170429A JP2681802B2 (en) 1988-07-08 1988-07-08 Combustor
EP92105621A EP0493376B1 (en) 1988-07-08 1989-07-06 Combustion apparatus
EP89112363A EP0350032B1 (en) 1988-07-08 1989-07-06 Combustion apparatus
DE1989624539 DE68924539T2 (en) 1988-07-08 1989-07-06 Incinerator.
DE1989609851 DE68909851T2 (en) 1988-07-08 1989-07-06 Incinerator.
US07/814,226 US5203690A (en) 1988-07-08 1991-12-23 Combustion apparatus
US07/850,649 US5232358A (en) 1988-07-08 1992-03-13 Combustion apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63170429A JP2681802B2 (en) 1988-07-08 1988-07-08 Combustor

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP8812097A Division JP2802616B2 (en) 1997-04-07 1997-04-07 Combustor

Publications (2)

Publication Number Publication Date
JPH0221105A true JPH0221105A (en) 1990-01-24
JP2681802B2 JP2681802B2 (en) 1997-11-26

Family

ID=15904754

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63170429A Expired - Lifetime JP2681802B2 (en) 1988-07-08 1988-07-08 Combustor

Country Status (1)

Country Link
JP (1) JP2681802B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002249302A (en) * 2001-02-16 2002-09-06 Nippon Chem Plant Consultant:Kk Method and apparatus for reforming by internal heating- type oxidation

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50150933A (en) * 1974-05-27 1975-12-04
JPS54168645U (en) * 1978-05-19 1979-11-28
JPS6263523U (en) * 1985-08-26 1987-04-20

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50150933A (en) * 1974-05-27 1975-12-04
JPS54168645U (en) * 1978-05-19 1979-11-28
JPS6263523U (en) * 1985-08-26 1987-04-20

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002249302A (en) * 2001-02-16 2002-09-06 Nippon Chem Plant Consultant:Kk Method and apparatus for reforming by internal heating- type oxidation

Also Published As

Publication number Publication date
JP2681802B2 (en) 1997-11-26

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