JPH0361086B2 - - Google Patents
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- Publication number
- JPH0361086B2 JPH0361086B2 JP61016726A JP1672686A JPH0361086B2 JP H0361086 B2 JPH0361086 B2 JP H0361086B2 JP 61016726 A JP61016726 A JP 61016726A JP 1672686 A JP1672686 A JP 1672686A JP H0361086 B2 JPH0361086 B2 JP H0361086B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- exhaust gas
- furnace
- combustion furnace
- cooling section
- 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 - Lifetime
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- Incineration Of Waste (AREA)
- Chimneys And Flues (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、燃焼排ガス冷却部を燃焼炉と一体に
備えた燃焼装置の運転方法及び燃焼装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method of operating a combustion apparatus including a combustion exhaust gas cooling section integrally with a combustion furnace, and a combustion apparatus.
従来、ボイラ、空気予熱器または水噴霧ガス冷
却室などの燃焼炉から排出する排ガスを冷却する
燃焼排ガス冷却部を備えた燃焼炉では燃焼排ガス
冷却部は燃焼炉から独立した機器として燃焼炉か
ら離して設置され、耐火物を内張りしたダクトに
よつて互いに連結されていた。
Conventionally, in combustion furnaces equipped with a flue gas cooling section that cools the flue gas discharged from the combustion furnace, such as a boiler, air preheater, or water spray gas cooling chamber, the flue gas cooling section is separated from the combustion furnace as an independent device. They were installed together and connected to each other by ducts lined with refractory material.
従つて、膨大な設置面積が必要となり、その
上、燃焼炉、接続ダクト、燃焼排ガス冷却部に対
する支持架構、点検用歩廊等を設置しなければな
らず、また、接続ダクト、燃焼炉出口、燃焼排ガ
ス冷却部入口等の煙道における排ガス流の乱れに
伴う圧力損失や、ダクトの堆積、付着などが避け
られない等の問題があつた。 Therefore, a huge installation area is required, and in addition, it is necessary to install a combustion furnace, a connecting duct, a support structure for the combustion exhaust gas cooling section, a walkway for inspection, etc. There were problems such as pressure loss due to turbulence of the exhaust gas flow in the flue such as the entrance of the exhaust gas cooling section, and unavoidable accumulation and adhesion on the duct.
また、ダスト溶融による接続ダクトでのトラブ
ルを防ぐために炉出口排ガス温度を炉頂水噴霧や
冷却用送風機による冷気吹込等により通常900〜
1000℃まで冷却する必要があり、従つて排ガス冷
却を空気予熱器やボイラなどを用いる場合のよう
に熱回収により行うときにはその分回収熱量が少
なくなつてしまう欠点もあつた。 In addition, in order to prevent troubles in the connecting ducts due to dust melting, the temperature of the exhaust gas at the furnace outlet is usually kept at 900 to
It is necessary to cool the exhaust gas to 1000°C, so when exhaust gas is cooled by heat recovery, such as when using an air preheater or boiler, there is a drawback that the amount of recovered heat is reduced accordingly.
そこで、最近では、第3図に示すように燃焼排
ガス冷却部2を燃焼炉1の上に載置し、燃焼炉1
のフリーボード部の天井がそのまま燃焼排ガス冷
却部2の入口となるように一体化した燃焼装置が
実用化されつつある。 Therefore, recently, the combustion exhaust gas cooling unit 2 is placed on top of the combustion furnace 1 as shown in FIG.
Combustion devices that are integrated so that the ceiling of the freeboard section directly serves as the inlet of the combustion exhaust gas cooling section 2 are being put into practical use.
これにより、設備の設置面積は燃焼排ガス冷却
部の分が全く不要となり、接続ダクトが無くな
り、支持架構は燃焼炉の分だけで済み、点検歩廊
は燃焼炉や冷却部ケーシングから張り出したもの
だけで間に合い、燃焼排ガス流の乱れもほとんど
無くなり、従つて、燃焼排ガスの通風圧力損失や
ダストの堆積、付着などが軽減され、メンテナン
ス上の問題が軽減され、通風のための動力も低下
した。 As a result, the installation area of the equipment for the combustion exhaust gas cooling section is completely unnecessary, there are no connecting ducts, the support frame is only needed for the combustion furnace, and the inspection walkway is only the one that protrudes from the combustion furnace and cooling section casing. In time, there was almost no turbulence in the flow of combustion exhaust gas, which reduced ventilation pressure loss of combustion exhaust gas, dust accumulation and adhesion, reduced maintenance problems, and reduced the power required for ventilation.
しかしながら、燃焼炉1と燃焼排ガス冷却部2
を一体化すると、燃焼炉1から輻射の形で多量の
熱が燃焼排ガス冷却部2に伝達される結果、燃焼
炉1内の温度が低下し、このことはある燃焼物に
とつては有利であるが、別の燃焼物にとつては却
つて不都合となり、場合によりこのような一体化
炉を使用することができないこともあつた。
However, the combustion furnace 1 and the combustion exhaust gas cooling section 2
When integrated, a large amount of heat is transferred from the combustion furnace 1 in the form of radiation to the flue gas cooling section 2, resulting in a decrease in the temperature inside the combustion furnace 1, which may be advantageous for certain combustion materials. However, it was rather inconvenient for other combustion materials, and in some cases such an integrated furnace could not be used.
即ち、発熱量の高い燃焼物の場合には、炉頂水
噴霧や冷気吹込等による炉の冷却負荷が軽減さ
れ、さらに燃焼排ガスの冷却にボイラや空気予熱
器を用いた場合には炉の冷却をしなくてよい分だ
け回収可能の熱量が増加する上、輻射により多量
の伝熱を受けるためボイラや空気予熱器の伝熱面
積を増大しなくて済むという点で好都合である。
加えて炉の冷却負荷が軽減した分排ガス風量も小
さくなり、排ガス処理設備や排ガス通風動力、煙
突口径等排ガス関係の設備容量をすべて小さくで
きるという利点もある。 In other words, in the case of combustible materials with a high calorific value, the cooling load on the furnace is reduced by water spraying at the top of the furnace, cold air injection, etc., and furthermore, when a boiler or air preheater is used to cool the combustion exhaust gas, the cooling load on the furnace is reduced. This is advantageous in that the amount of heat that can be recovered increases by the amount of heat that is not required, and there is no need to increase the heat transfer area of the boiler or air preheater because a large amount of heat is transferred by radiation.
In addition, since the cooling load on the furnace is reduced, the amount of exhaust gas airflow is also reduced, and there is the advantage that the capacity of all exhaust gas-related equipment such as exhaust gas treatment equipment, exhaust gas ventilation power, and chimney diameter can be reduced.
しかしその一方、発熱量の少ない燃焼物の場合
や部分負荷運転には、燃焼排ガス冷却部からの熱
伝達により燃焼炉内が冷却され、炉内を燃焼や有
害物質、悪臭等の分解に必要な温度に保持するた
め、助燃剤を使用しなければならなくなつたりそ
の量を増加したりすることが必要になるという問
題点を有する。 On the other hand, however, in the case of combustible materials with a low calorific value or during partial load operation, the inside of the combustion furnace is cooled by heat transfer from the flue gas cooling section, and the inside of the furnace is cooled to perform combustion and decompose harmful substances and bad odors. In order to maintain the temperature, there is a problem in that it becomes necessary to use or increase the amount of combustion improver.
殊に、最近問題となつているダイオキシンやベ
ンツピレン等有害な有機塩素化合物を除去するに
は分解温度以上の温度で加熱して分解する必要が
ある。しかし、ダイオキシンなどこれらの化合物
はその分解温度900〜1200℃と高いので燃焼排ガ
ス流路におけるダストの溶融付着や材料の耐熱性
の問題によりこの高温を適用するのは困難であ
る、という問題点を有した。 In particular, in order to remove harmful organic chlorine compounds such as dioxins and benzpyrene, which have recently become a problem, it is necessary to decompose them by heating at a temperature higher than the decomposition temperature. However, these compounds such as dioxins have a high decomposition temperature of 900 to 1200°C, so it is difficult to apply this high temperature due to the melting and adhesion of dust in the flue gas flow path and the heat resistance of the materials. I had it.
本発明は、上記の従来の問題点を解決し、発熱
量が低い場合にも助燃剤を要さず、また高温燃焼
を行いながら燃焼排ガス流路のダスト溶着や材料
選択の問題のない燃焼炉と燃焼排ガス冷却部とを
一体化した燃焼装置の運転方法及び燃焼装置を提
供することを目的としている。 The present invention solves the above-mentioned conventional problems, and provides a combustion furnace that does not require a combustion improver even when the calorific value is low, and that does not require dust welding in the flue gas flow path or material selection problems while performing high-temperature combustion. The object of the present invention is to provide a method for operating a combustion apparatus and a combustion apparatus in which a combustion apparatus and a combustion exhaust gas cooling section are integrated.
本発明は、上記の問題点を解決する手段とし
て、燃焼炉と燃焼排ガス冷却部とを一体化した燃
焼装置の運転方法において、燃焼炉から燃焼排ガ
ス冷却部へ輻射伝熱により移動する熱量を燃焼炉
内の温度に応じて熱通過面積により常時調節して
燃焼炉内温度を調節することを特徴とする燃焼装
置の運転方法、及び燃焼炉と燃焼排ガス冷却部と
を一体化した燃焼装置において、燃焼炉と燃焼排
ガス冷却部との接続部付近の燃焼排ガス流路中に
前記燃焼炉から前記燃焼排ガス冷却部への輻射伝
熱を遮蔽する面積が燃焼炉内の温度に応じて常時
調節可能な輻射伝熱遮蔽体を設けたことを特徴と
する燃焼装置を提供せんとするものである。
As a means to solve the above-mentioned problems, the present invention provides a method for operating a combustion apparatus that integrates a combustion furnace and a combustion exhaust gas cooling section, in which the amount of heat transferred from the combustion furnace to the combustion exhaust gas cooling section by radiant heat transfer is reduced by combustion. A method of operating a combustion device characterized in that the temperature inside the combustion furnace is adjusted by constantly adjusting the heat passage area according to the temperature inside the furnace, and a combustion device in which the combustion furnace and the combustion exhaust gas cooling section are integrated, An area that shields radiant heat transfer from the combustion furnace to the combustion exhaust gas cooling section in the combustion exhaust gas flow path near the connection between the combustion furnace and the combustion exhaust gas cooling section can be constantly adjusted according to the temperature inside the combustion furnace. It is an object of the present invention to provide a combustion device characterized by being provided with a radiation heat transfer shield.
本発明の実施例につき図面を用して説明する。 Embodiments of the present invention will be described with reference to the drawings.
第1図及び第2図において、燃焼炉1の上に
は、ガス冷却室、ボイラまたは空気予熱器などの
輻射伝熱面である燃焼排ガス冷却部2が一体に載
置されている。燃焼炉1と燃焼排ガス冷却部2と
の接続部は横断面がほぼ長方形であり、その付近
の燃焼排ガス流路中には、横方向にほぼ同一横断
面の可動翼3群が輻射伝熱遮蔽体として設置され
ている。可動翼3は厚さに対して巾が大の板状材
で、長手方向の一端または両端にて炉壁を貫通す
る回転軸4で支えられている。該回転軸4は炉外
で駆動機5に接続され、遠隔操作で信号により回
転可能とされている。 In FIGS. 1 and 2, a combustion exhaust gas cooling section 2, which is a radiation heat transfer surface of a gas cooling chamber, a boiler, an air preheater, etc., is integrally placed on top of a combustion furnace 1. The connecting part between the combustion furnace 1 and the flue gas cooling unit 2 has a nearly rectangular cross section, and in the flue gas flow path in the vicinity thereof, three groups of movable blades with approximately the same cross section in the lateral direction provide radiation heat transfer shielding. It is installed as a body. The movable blade 3 is a plate-shaped member whose width is large relative to its thickness, and is supported at one or both ends in the longitudinal direction by a rotating shaft 4 that penetrates the furnace wall. The rotating shaft 4 is connected to a driving machine 5 outside the furnace, and can be rotated by remote control using a signal.
可動翼3群は各回転軸4の回転により輻射伝熱
を遮蔽する面積即ち、燃焼炉1と燃焼排ガス冷却
部2との接続面に対する投影面積が大きく変化
し、且つ投影面積の最大となるいわゆる閉じた状
態では投影面がほぼ接続面全体を蔽うように、水
平方向の間隔をあけて設けられる。また高さも交
互にずらして設け、閉じた状態においても燃焼排
ガス流路を閉塞しないようにしてあつて、燃焼排
ガスの燃焼炉1からの流出を阻害することがな
く、従つて圧力損失を生ずることのないようにし
てある。投影面積の小さいいわゆる開いた状態は
閉じた状態に対し約90゜回転軸4を回転させて得
られる。 The movable blade group 3 has a so-called area where the area for shielding radiation heat transfer due to the rotation of each rotating shaft 4, that is, the projected area with respect to the connection surface between the combustion furnace 1 and the combustion exhaust gas cooling section 2 changes greatly, and the projected area is the maximum. In the closed state, the projection surfaces are spaced apart in the horizontal direction so that they cover almost the entire connection surface. In addition, the heights are alternately staggered so as not to block the combustion exhaust gas flow path even in the closed state, so that the outflow of the combustion exhaust gas from the combustion furnace 1 is not obstructed, and therefore no pressure loss occurs. It is made so that there is no The so-called open state with a small projected area can be obtained by rotating the rotation axis 4 by about 90 degrees with respect to the closed state.
可動翼3は単板でもよいが、燃焼炉1に臨む面
と燃焼排ガス冷却部2に臨む面との温度差による
応力を下げるよう、多孔体としたり、複板や中空
とするなど工夫することが好ましい。これは輻射
熱の遮断性の向上にも役立つものである。また、
可動翼3の特に燃焼炉1に臨む面は、燃焼炉1か
らの熱により炉内温度に近い温度となつて自らも
熱輻射を行つて受けた熱を炉内に返すようにする
のが炉内を高温に維持するのに効果的である。従
つて、高温維持の面からいえば炉内温度に耐える
耐火材製として、冷却機構を設けない方がよい
が、必要に応じて冷却媒体を流過することができ
るようにしてもよい。 The movable blade 3 may be a single plate, but in order to reduce the stress caused by the temperature difference between the surface facing the combustion furnace 1 and the surface facing the combustion exhaust gas cooling section 2, it may be made of a porous body, a multi-plate, or hollow. is preferred. This also helps improve the ability to block radiant heat. Also,
Particularly, the surface of the movable blade 3 facing the combustion furnace 1 reaches a temperature close to the temperature inside the furnace due to the heat from the combustion furnace 1, and it also radiates heat and returns the received heat to the inside of the furnace. Effective in maintaining high temperature inside. Therefore, from the viewpoint of maintaining high temperature, it is better to use a refractory material that can withstand the temperature inside the furnace and not provide a cooling mechanism, but it may be possible to allow a cooling medium to flow through it as necessary.
また厚さが巾と比べて薄く横方向に長い翼状で
かつ回転も行うため、振動や歪みも生じ、自重や
熱応力もかかることから、機械的強度も持たせな
くてはならない。従つて、回転軸4を水冷ないし
空冷とし、それにいくつかに分割した耐火材の翼
部からなる可動翼3を取り付けたり、機械強度を
持つ炭化ケイ素系や窒化ケイ素系のセラミツク製
の回転軸4及び可動翼3とすることが望ましい。
セラミツク製とする場合は高温での機械強度、耐
熱衝撃性、耐熱性、耐酸化性等の秀れた性質をも
つているβ−SiCが特に好ましい。 Furthermore, since it is thinner than its width and has a wing-like shape that is long in the lateral direction, and also rotates, it is subject to vibration and distortion, and is subject to its own weight and thermal stress, so it must also have mechanical strength. Therefore, the rotary shaft 4 may be water-cooled or air-cooled, and a movable blade 3 made of a refractory material wing section divided into several parts may be attached to it, or the rotary shaft 4 may be made of silicon carbide-based or silicon nitride-based ceramic having mechanical strength. and a movable wing 3.
When made of ceramic, β-SiC is particularly preferred as it has excellent properties such as mechanical strength at high temperatures, thermal shock resistance, heat resistance, and oxidation resistance.
しかして燃焼炉1の燃焼排ガス冷却部2への輻
射伝熱はこの可動翼3群の回転により無段階に調
節することができる。従つて燃焼炉1内の温度を
検出し駆動機5に操作信号を出力する温度調節器
6で燃焼温度を検出し、温度が高いときは開、低
いときは閉の信号を可動翼3群の駆動機5に送
り、可動翼3群を適宜回転させて燃焼炉1から燃
焼排ガス冷却部2への輻射伝熱を遮断する面積を
変え、よつて燃焼炉1内を所定の温度に調節する
ことが可能となる。 Therefore, the radiation heat transfer to the combustion exhaust gas cooling section 2 of the combustion furnace 1 can be adjusted steplessly by rotating the group of movable blades 3. Therefore, the combustion temperature is detected by the temperature regulator 6 which detects the temperature inside the combustion furnace 1 and outputs an operation signal to the drive unit 5. When the temperature is high, the combustion temperature is detected, and when the temperature is low, the signal to open is sent to the three groups of movable blades. Send it to the driving machine 5 and rotate the 3 groups of movable blades as appropriate to change the area that blocks radiation heat transfer from the combustion furnace 1 to the flue gas cooling section 2, thereby adjusting the inside of the combustion furnace 1 to a predetermined temperature. becomes possible.
即ち、可動翼3群が閉じた状態では燃焼炉1内
からの輻射熱はほとんどが可動翼3群にさえぎら
れる。可動翼3群の焼却炉1に臨んだ面は燃焼炉
1内と同様の高温となつており、受熱量に近い熱
を輻射し燃焼炉1に戻してしまう。即ち、可動翼
3群は熱反射板的作用を行う。開いた状態では隙
間から輻射熱が燃焼排ガス冷却部2に入る。該部
は冷却されているために燃焼炉1に熱は戻らず、
燃焼炉1は冷却されることになる。燃焼炉1から
の輻射熱は絶対温度の4乗に比例して増加するた
め、炉内温度を抑制する効果は大きい。この隙間
の大きさを無段階に調節することで容易に炉内温
度を調節することができる。 That is, when the three groups of movable blades are closed, most of the radiant heat from inside the combustion furnace 1 is blocked by the three groups of movable blades. The surface of the three groups of movable blades facing the incinerator 1 has a high temperature similar to that inside the combustion furnace 1, and radiates heat close to the amount of heat received and returns it to the combustion furnace 1. That is, the three groups of movable blades act like a heat reflector. In the open state, radiant heat enters the combustion exhaust gas cooling section 2 through the gap. Since this part is cooled, no heat returns to the combustion furnace 1,
The combustion furnace 1 will be cooled. Since the radiant heat from the combustion furnace 1 increases in proportion to the fourth power of the absolute temperature, the effect of suppressing the temperature inside the furnace is large. By steplessly adjusting the size of this gap, the temperature inside the furnace can be easily adjusted.
さらに、燃焼炉1が高温の時に高温の燃焼排ガ
スが燃焼排ガス冷却部2に直ちに流入しても、燃
焼炉1が高温の場合は可動翼3群により燃焼炉1
からの輻射伝熱は遮断されているので該燃焼排ガ
ス冷却部2は冷却能力を十分保持しているので、
流入したと同時に急冷される。従つて、燃焼排ガ
スに含まれる飛灰が一部溶けたり焼結を始めるよ
うな高温により燃焼を行つても燃焼灰ガスは燃焼
排ガス冷却部2に移ると同時に冷却されて付着性
のなくなる温度まで直ちに降温し、燃焼排ガス通
路に付着して通路を閉塞したり燃焼排ガス冷却部
2冷却伝熱面やノズルにスケールを形成してトラ
ブルや能力低下を引き起こすこともないので、高
温燃焼が可能となる。従つて、都市ごみ焼却の場
合、従来の950℃以下の燃焼温度ではダイオキシ
ン等の難燃性の有毒有機塩素化合物が分解されな
い危険があつたが、1000〜1200℃以上で燃焼させ
ることによつてそれら有害物質も分解除去でき
る。 Furthermore, even if high-temperature flue gas immediately flows into the flue gas cooling unit 2 when the combustion furnace 1 is at a high temperature, if the combustion furnace 1 is at a high temperature, the movable blades 3
Since the radiant heat transfer from the combustion exhaust gas cooling section 2 has sufficient cooling capacity,
As soon as it flows in, it is rapidly cooled down. Therefore, even if combustion is performed at such high temperatures that some of the fly ash contained in the flue gas melts or begins to sinter, the flue gas is cooled as soon as it moves to the flue gas cooling section 2 to a temperature at which it no longer sticks. The temperature drops immediately, and high-temperature combustion is possible because it does not adhere to the combustion exhaust gas passage and block the passage or form scale on the cooling heat transfer surface of the combustion exhaust gas cooling unit 2 or the nozzle, causing trouble or a reduction in performance. . Therefore, in the case of municipal waste incineration, there was a risk that flame-retardant toxic organic chlorine compounds such as dioxins would not be decomposed at conventional combustion temperatures of 950℃ or lower, but by incinerating them at temperatures of 1000 to 1200℃ or higher, These harmful substances can also be decomposed and removed.
なお、燃焼炉1が流動床燃焼炉の場合は流動床
では燃焼率を抑えて800〜850℃以下とし、その上
部空間のフリーボード部において1000〜1200℃以
上で燃焼させれば、炉床も従来のもので対応でき
る。 In addition, if the combustion furnace 1 is a fluidized bed combustion furnace, the combustion rate in the fluidized bed is suppressed to 800 to 850℃ or less, and if the combustion is performed at 1000 to 1200℃ or higher in the freeboard part of the upper space, the hearth also Conventional products can be used.
また、発熱量の少ない燃焼物の場合や部分負荷
運転の場合でも可動翼3群を閉じることにより燃
焼炉1からの熱の流出を防ぎ燃焼排ガス冷却部2
による冷却を防ぐことができるので、助燃剤を入
れなくとも高温を得ることが可能となる。 In addition, even in the case of a combustible material with a low calorific value or in partial load operation, the 3 groups of movable blades are closed to prevent heat from escaping from the combustion furnace 1 and the combustion exhaust gas cooling section 2
Since it is possible to prevent cooling caused by combustion, it is possible to obtain a high temperature without adding a combustion improver.
以上、投影面のほぼ全体を蔽うことが可能の可
動翼3とした例で説明したが、最大遮断状態で必
ずしも投影面の全体を蔽う輻射伝熱遮蔽体でなく
ともよい。 Although the movable blade 3 has been described above as an example that can cover almost the entire projection surface, the radiation heat transfer shield does not necessarily have to cover the entire projection surface in the maximum shielding state.
本発明は、燃焼炉から燃焼排ガス冷却部へ輻射
伝熱により移動する熱量を燃焼炉内の温度に応じ
て熱通過面積により常時調節して燃焼炉内温度を
調節することにより、燃焼炉からの熱の流出を防
ぎ、燃焼炉内の温度が低下することなく安定した
運転が可能であり、高温燃焼が焼却物の状態に応
じてでき難燃性の有毒物質の分解除去をも容易で
きると共に、部分負荷運転にも効果的に対応で
き、発熱量が低い場合にも助熱剤を要さず、また
は節約することができ、また高温燃焼を行いなが
ら燃焼排ガス流路のダスト溶着や材料選択の問題
のない燃焼装置の運転方法及び燃焼装置を提供で
き、実用上顕著な効果を奏することができる。
The present invention constantly adjusts the amount of heat transferred from the combustion furnace to the flue gas cooling section by radiation heat transfer according to the temperature inside the combustion furnace by the heat passage area, thereby adjusting the temperature inside the combustion furnace. It prevents heat leakage, enables stable operation without lowering the temperature inside the combustion furnace, and enables high-temperature combustion depending on the condition of the incinerated material, making it easy to decompose and remove flame-retardant toxic substances. It can effectively handle partial load operation, eliminates or saves heat additives even when the calorific value is low, and can reduce dust welding in the flue gas flow path and material selection while performing high-temperature combustion. It is possible to provide a method for operating a combustion device and a combustion device without any problems, and it is possible to achieve significant practical effects.
第1図及び第2図は本発明の実施例を示し、第
1図はフロー図、第2図は第1図−線断面平
面図、第3図は従来例の正面図である。
1……燃焼炉、2……燃焼排ガス冷却部、3…
…可動翼、4……回転軸、5……駆動機、6……
温度調節器。
1 and 2 show an embodiment of the present invention, FIG. 1 is a flow diagram, FIG. 2 is a sectional plan view taken along the line of FIG. 1, and FIG. 3 is a front view of a conventional example. 1... Combustion furnace, 2... Combustion exhaust gas cooling section, 3...
...Movable wing, 4...Rotating shaft, 5...Driver, 6...
air conditioner.
Claims (1)
焼装置の運転方法において、燃焼炉から燃焼排ガ
ス冷却部へ輻射伝熱により移動する熱量を燃焼炉
内の温度に応じて熱通過面積により常時調節して
燃焼炉内温度を調節することを特徴とする燃焼装
置の運転方法。 2 燃焼炉と燃焼排ガス冷却部とを一体化した燃
焼装置において、燃焼炉と燃焼排ガス冷却部との
接続部付近の燃焼排ガス流路中に前記燃焼炉から
前記燃焼排ガス冷却部への輻射伝熱を遮蔽する面
積が燃焼炉内の温度に応じて常時調節可能な輻射
伝熱遮蔽体を設けたことを特徴とする燃焼装置。 3 前記輻射伝熱遮蔽体が、可動翼である特許請
求の範囲第2項記載の燃焼装置。[Claims] 1. In a method of operating a combustion device that integrates a combustion furnace and a combustion exhaust gas cooling section, the amount of heat transferred from the combustion furnace to the combustion exhaust gas cooling section by radiation heat transfer is controlled according to the temperature inside the combustion furnace. A method of operating a combustion apparatus, characterized in that the temperature inside the combustion furnace is adjusted by constantly adjusting the heat passage area. 2. In a combustion device that integrates a combustion furnace and a combustion exhaust gas cooling section, radiant heat transfer from the combustion furnace to the combustion exhaust gas cooling section occurs in the combustion exhaust gas flow path near the connection between the combustion furnace and the combustion exhaust gas cooling section. 1. A combustion device characterized by being provided with a radiation heat transfer shield whose area for shielding can be constantly adjusted according to the temperature within the combustion furnace. 3. The combustion apparatus according to claim 2, wherein the radiation heat transfer shield is a movable blade.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1672686A JPS62175511A (en) | 1986-01-30 | 1986-01-30 | Method for operating combustion device and combustion device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1672686A JPS62175511A (en) | 1986-01-30 | 1986-01-30 | Method for operating combustion device and combustion device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62175511A JPS62175511A (en) | 1987-08-01 |
| JPH0361086B2 true JPH0361086B2 (en) | 1991-09-18 |
Family
ID=11924263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1672686A Granted JPS62175511A (en) | 1986-01-30 | 1986-01-30 | Method for operating combustion device and combustion device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62175511A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5257585A (en) * | 1991-04-15 | 1993-11-02 | Ebara Corporation | Incinerator |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52126970A (en) * | 1976-04-19 | 1977-10-25 | Nippon Kokan Kk <Nkk> | Double ceiling for refuse incinerator |
| JPS58214701A (en) * | 1982-06-09 | 1983-12-14 | フオスタ−・ホイ−ラ−・エナ−ジイ・コ−ポレイシヨン | Fluidized-bed heat exchanger to which baffle plate device is arranged |
| JPS61195208A (en) * | 1985-02-25 | 1986-08-29 | Ebara Corp | Incinerator |
-
1986
- 1986-01-30 JP JP1672686A patent/JPS62175511A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62175511A (en) | 1987-08-01 |
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