JPH07260122A - Method and device for stabilized combustion in fluidizerd bed furnace - Google Patents
Method and device for stabilized combustion in fluidizerd bed furnaceInfo
- Publication number
- JPH07260122A JPH07260122A JP7819994A JP7819994A JPH07260122A JP H07260122 A JPH07260122 A JP H07260122A JP 7819994 A JP7819994 A JP 7819994A JP 7819994 A JP7819994 A JP 7819994A JP H07260122 A JPH07260122 A JP H07260122A
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- exhaust gas
- bed furnace
- combustion
- temperature
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、発熱量が比較的高い都
市ごみ、産業廃棄物、石炭等を流動床炉にて安定燃焼さ
せる方法及び装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for stably burning municipal waste, industrial waste, coal, etc., which have a relatively high calorific value, in a fluidized bed furnace.
【０００２】[0002]
【従来の技術】従来、流動床炉においては、流動媒体と
して、砂等が用いられており、流動層の温度は６００〜
６５０℃の範囲に入るように制御されている。被処理物
の燃焼により流動層温度が上昇するので、従来、流動床
炉の冷却は、炉内に注水することにより行われている
（例えば、特開平４−３９５０９号公報参照）。また、
特開昭６１−１４９７１１号公報には、排ガスを空気と
ともに風箱に供給して、流動層温度の急速な制御を行う
ことができるようにした流動床炉が記載されている。2. Description of the Related Art Conventionally, sand or the like has been used as a fluid medium in a fluidized bed furnace, and the temperature of the fluidized bed is 600 to 600.
It is controlled to be in the range of 650 ° C. Since the temperature of the fluidized bed rises due to the combustion of the object to be treated, cooling of the fluidized bed furnace is conventionally performed by pouring water into the furnace (see, for example, JP-A-4-39509). Also,
Japanese Unexamined Patent Publication No. 61-149711 describes a fluidized bed furnace in which exhaust gas is supplied together with air to a wind box so that the fluidized bed temperature can be rapidly controlled.
【０００３】図６は、従来の水注入方式の流動床炉１０
を示している。１２は流動層、１４は流動層に接続され
た温度検出制御手段、１６は空気押込ファン、１８は不
燃物排出導管である。図６に示す流動床炉においては、
炉内に注水することにより炉内温度を低下させる。この
場合、注水ライン２０の水量調節弁２２と温度検出制御
手段１４とを接続して、流動層１２の温度が一定範囲に
入るように注水量を制御する。FIG. 6 shows a conventional water injection type fluidized bed furnace 10.
Is shown. Reference numeral 12 is a fluidized bed, 14 is temperature detection control means connected to the fluidized bed, 16 is an air pushing fan, and 18 is an incombustibles discharge conduit. In the fluidized bed furnace shown in FIG.
The temperature inside the furnace is lowered by pouring water into the furnace. In this case, the water amount control valve 22 of the water injection line 20 and the temperature detection control means 14 are connected to control the water injection amount so that the temperature of the fluidized bed 12 falls within a certain range.
【０００４】[0004]
【発明が解決しようとする課題】図６に示す従来の注水
方式の流動床炉では、炉内に注水して流動層温度を冷却
するので、水の潜熱分、炉出口温度が低下し過ぎ、ＣＯ
低減、ダイオキシン低減のための高温燃焼に逆行するも
のである。高温を維持するためには、空気量を絞ること
になり、これが不完全燃焼の原因ともなるという問題点
があった。また、燃焼排ガス冷却装置がボイラ方式の場
合は、注水により、ボイラ蒸発量が減少するという欠点
があった。In the conventional fluidized bed fluidized bed furnace shown in FIG. 6, water is poured into the furnace to cool the temperature of the fluidized bed, so that the latent heat of water and the temperature at the exit of the furnace are too low. CO
It goes against high temperature combustion for reduction and reduction of dioxins. In order to maintain the high temperature, the amount of air is reduced, which causes a problem of incomplete combustion. Further, when the combustion exhaust gas cooling device is of a boiler type, there is a drawback that the amount of evaporation of the boiler decreases due to water injection.
【０００５】また、流動層内に、空気とともに排ガスを
供給する場合は、炉内温度が低下して注水量を減少させ
ることができるが、投入廃棄物等の燃料の燃焼が不完全
になるという問題がある。とくに、投入廃棄物等の燃料
の負荷が変動すると、この影響が大きく、安定な燃焼を
実施することが難しかった。Further, when the exhaust gas is supplied into the fluidized bed together with the air, the temperature inside the furnace can be lowered to reduce the amount of water injection, but the combustion of fuel such as input waste becomes incomplete. There's a problem. In particular, when the load of fuel such as input waste fluctuates, this influence is great and it is difficult to carry out stable combustion.
【０００６】本発明は上記の諸点に鑑みなされたもの
で、本発明の目的は、流動床炉の被処理物投入ゾーンの
風箱のみに排ガス再循環用ガスを導入して流動媒体を流
動化させることにより、投入された被処理物をゆるやか
に燃焼させ、被処理物の負荷変動の影響を小さくして、
完全燃焼及び安定燃焼を図るとともに、炉内冷却のため
の注水量の低減を図ることができる流動床炉における安
定燃焼方法及び装置を提供することにある。The present invention has been made in view of the above points, and an object of the present invention is to fluidize a fluid medium by introducing an exhaust gas recirculation gas into only a wind box in a treatment object charging zone of a fluidized bed furnace. By doing so, the input processing object is gently burned, and the effect of load fluctuation of the processing object is reduced,
An object of the present invention is to provide a stable combustion method and apparatus in a fluidized bed furnace capable of achieving complete combustion and stable combustion and reducing the amount of water injection for cooling the furnace.
【０００７】[0007]
【課題を解決するための手段及び作用】上記の目的を達
成するために、本発明の流動床炉における安定燃焼方法
は、図１及び図２に示すように、流動床炉１０の被処理
物投入ゾーンＡの流動層下側の風箱２４に、熱回収後の
冷却された燃焼排ガスを循環・供給し、風箱の他の部分
には空気を供給して流動媒体を流動化させることを特徴
としている。なお、被処理物投入ゾーンＡの風箱２４は
被処理物投入ゾーン（廃棄物投入範囲）Ａより若干広く
なるように小風箱２４として形成することが好ましい。
しかし、この小風箱２４は必ずしも設置する必要はな
く、仕切をなくして小風箱２４の設置すべき位置に排ガ
スを導入するように構成することも可能である。２６は
空気分散板、２８は空気を導入する風箱、３０は排ガス
再循環ライン、３２は排ガス流量調節手段（弁、ダンパ
ー等）である。In order to achieve the above object, the method for stable combustion in a fluidized bed furnace of the present invention is as follows. As shown in FIG. 1 and FIG. The cooled combustion exhaust gas after heat recovery is circulated and supplied to the wind box 24 below the fluidized bed of the input zone A, and air is supplied to the other parts of the wind box to fluidize the fluidized medium. It has a feature. In addition, it is preferable that the wind box 24 in the processing object input zone A is formed as a small air box 24 so as to be slightly wider than the processing object input zone (waste input range) A.
However, the small wind box 24 does not necessarily have to be installed, and it is possible to eliminate the partition and introduce the exhaust gas to the position where the small wind box 24 should be installed. 26 is an air dispersion plate, 28 is a wind box for introducing air, 30 is an exhaust gas recirculation line, and 32 is an exhaust gas flow rate adjusting means (valve, damper, etc.).
【０００８】上記の方法において、温度制御手段１４と
排ガス流量調節手段３２とを接続して、排ガス供給量を
調節して被処理物投入ゾーンＡの流動層温度を制御する
ことができるように構成することが好ましい。また、燃
焼排ガス風量制御に最大及び最小の制限を設けることが
好ましい。In the above method, the temperature control means 14 and the exhaust gas flow rate adjusting means 32 are connected to each other so that the amount of exhaust gas supplied can be adjusted to control the temperature of the fluidized bed in the processing object charging zone A. Preferably. Further, it is preferable to set maximum and minimum limits for the combustion exhaust gas flow rate control.
【０００９】本発明の流動床炉における安定燃焼装置
は、図１及び図２に示すように、空気で流動化する流動
層１２を備えた流動床炉１０の被処理物投入ゾーンＡの
流動層１２下側に小風箱２４を設け、この小風箱２４に
熱回収後の冷却された燃焼排ガスを循環・供給するため
の、排ガス流量調節手段３２を備えた排ガス再循環ライ
ン３０を接続し、流動層１２に接続された温度制御手段
１４と前記排ガス流量調節手段３２とを、排ガス流量に
より流動層温度を制御するように接続したことを特徴と
している。温度制御手段１４は、被処理物投入ゾーンＡ
の流動層１２に接続することが好ましい。The stable combustion apparatus in the fluidized bed furnace of the present invention is, as shown in FIGS. 1 and 2, a fluidized bed in an object-to-be-processed zone A of a fluidized bed furnace 10 having a fluidized bed 12 fluidized by air. 12 is provided with a small air box 24, and an exhaust gas recirculation line 30 equipped with an exhaust gas flow rate adjusting means 32 for circulating and supplying the cooled combustion exhaust gas after heat recovery is connected to the small air box 24. The temperature control means 14 connected to the fluidized bed 12 and the exhaust gas flow rate adjusting means 32 are connected so as to control the temperature of the fluidized bed according to the exhaust gas flow rate. The temperature control means 14 is provided in the processing object charging zone A.
It is preferable to connect to the fluidized bed 12.
【００１０】上記のように、被処理物投入ゾーンＡの小
風箱２４又はこの部分の風箱のみに冷却された燃焼排ガ
ス（酸素濃度約１０％）を供給し、他のゾーンＢの風箱
２８には空気（酸素濃度２１％）を供給する。このた
め、ゾーンＡでは被処理物の燃焼が抑制され、ゾーンＢ
では、ゾーンＡで一部ガス化して拡散してきた被処理物
が、空気中の酸素で安定燃焼する。As described above, the cooled flue gas (oxygen concentration of about 10%) is supplied only to the small air box 24 in the object input zone A or the air box in this portion, and the air boxes in the other zones B are supplied. Air (oxygen concentration 21%) is supplied to 28. Therefore, in the zone A, the combustion of the object to be treated is suppressed, and in the zone B
Then, the object to be treated, which is partially gasified and diffused in the zone A, is stably burned by oxygen in the air.
【００１１】[0011]
【実施例】以下、本発明を実施例に基づいてさらに詳細
に説明するが、本発明は下記実施例に何ら限定されるも
のではなく、適宜変更して実施することが可能なもので
ある。図３は、本発明の流動床炉における安定燃焼方法
を実施する装置の一実施例を示している。流動床炉１０
の流動層１２から不燃物を含む砂等の流動媒体は、不燃
物排出導管１８により抜き出され、篩等の分級装置（図
示略）で大径の不燃物と流動媒体とに分離され、不燃物
は系外に排出され、流動媒体は流動床炉１０に循環され
る。EXAMPLES The present invention will be described in more detail based on the following examples, but the invention is not intended to be limited to the following examples, and various modifications can be made as appropriate. FIG. 3 shows an embodiment of an apparatus for carrying out the stable combustion method in the fluidized bed furnace of the present invention. Fluidized bed furnace 10
A fluid medium such as sand containing an incombustible substance is extracted from the fluidized bed 12 of No. 2 through an incombustible substance discharge conduit 18 and separated into a large-diameter incombustible substance and a fluid medium by a classifying device (not shown) such as a sieve, and the The substance is discharged to the outside of the system, and the fluidized medium is circulated in the fluidized bed furnace 10.
【００１２】３４は廃棄物等の被処理物投入口で、この
投入口３４から投入された被処理物が落下する流動層上
の領域、すなわち被処理物投入ゾーンＡ（図４参照）の
流動層下側に小風箱２４を設ける。したがって、この小
風箱２４は、空気を供給する風箱２８内に設けられるこ
とになる。なお、図５に示すように、空気を供給する風
箱２８を仕切板３６により区画して小風箱２４ａを形成
してもよい。Reference numeral 34 is an inlet for an object to be treated such as waste, and the region in the fluidized bed where the object introduced from the inlet 34 falls, that is, the flow in the object-introducing zone A (see FIG. 4). A small wind box 24 is provided on the lower side of the layer. Therefore, the small wind box 24 is provided in the wind box 28 that supplies air. As shown in FIG. 5, the air box 28 for supplying air may be divided by the partition plate 36 to form the small air box 24a.
【００１３】３８はボイラ方式の熱交換器、空気予熱器
等の燃焼排ガス冷却装置、４０は脱硝装置、脱硫装置、
脱塵装置等の排ガス処理装置、４２は誘引ファン、４４
は排ガス再循環ファン、４６は煙突である。排ガス流量
調節手段３２には排ガス流量検出制御手段５０が接続さ
れ、この排ガス流量検出制御手段５０と、被処理物投入
ゾーンＡの流動層に接続された温度検出制御手段１４と
が接続されて、排ガス流量を調節することにより、被処
理物投入ゾーンＡの流動層温度が所定の範囲に入るよう
に制御されるようになっている。Reference numeral 38 is a combustion exhaust gas cooling device such as a boiler heat exchanger or air preheater, 40 is a denitration device, a desulfurization device,
An exhaust gas treatment device such as a dust removing device, 42 is an induction fan, 44
Is an exhaust gas recirculation fan, and 46 is a chimney. The exhaust gas flow rate detection control means 50 is connected to the exhaust gas flow rate control means 32, and the exhaust gas flow rate detection control means 50 and the temperature detection control means 14 connected to the fluidized bed of the processing object charging zone A are connected, By adjusting the flow rate of the exhaust gas, the temperature of the fluidized bed in the processing object input zone A is controlled to fall within a predetermined range.
【００１４】ゾーンＡの流動層１２の温度は、燃焼を安
定させるために、５５０〜７００℃、望ましくは６００
〜６５０℃の範囲に制御される必要がある。この範囲未
満であると、ガス化反応となるため、被処理物が充分燃
焼しなくなり、一方、この範囲を超えると、燃焼速度が
速すぎて、ＣＯ及びダイオキシンの発生量が増加する傾
向がある。本実施例では、上記のように、被処理物投入
域直下（ゾーンＡ）の小風箱２４又は２４ａに冷却され
た排ガス（例えば１５０〜２００℃前後）を再循環させ
ることにより、この部分のＯ2 分圧を下げ、ゆるやかな
燃焼をさせ、一部ガス化した被処理物がＯ2 分圧の高い
ゾーンＢに流動層内を横方向に攪拌されて移動し、層内
一様に均一な燃焼が行われ、総合的な完全燃焼が達成さ
れる。また、被処理物投入ゾーンＡの流動層の温度を最
適温度に制御するために、排ガス再循環量に最大（Ｈ）
及び最小（Ｌ）の制限を設け、これを主に、注水を補助
として流動層温度を制御する。The temperature of the fluidized bed 12 in zone A is 550 to 700 ° C., preferably 600 to stabilize combustion.
It needs to be controlled in the range of ˜650 ° C. If it is less than this range, a gasification reaction occurs, so that the object to be treated is not sufficiently combusted. On the other hand, if it exceeds this range, the burning rate tends to be too fast, and the amounts of CO and dioxin generated tend to increase. . In this embodiment, as described above, by recirculating the cooled exhaust gas (for example, around 150 to 200 ° C.) to the small air box 24 or 24a immediately below the processing object input area (zone A), The O 2 partial pressure is lowered to cause gentle combustion, and the partially gasified object moves laterally to the zone B where the O 2 partial pressure is high in the fluidized bed while being agitated in the lateral direction, and is uniformly distributed in the bed. Various combustions are performed, and total complete combustion is achieved. Further, in order to control the temperature of the fluidized bed in the processing object input zone A to the optimum temperature, the exhaust gas recirculation amount is set to the maximum (H).
And a minimum (L) limit, which mainly controls the fluidized bed temperature with the aid of water injection.
【００１５】このように、被処理物投入域部の小風箱に
排ガス再循環用排ガスを使用すると、この部分の燃焼用
酸素濃度が２１％から約１０％に低下するため、この部
分における流動層内での燃焼率が低下し、廃棄物の質、
廃棄物量の負荷変動を吸収しやすくなる。また、ゾーン
Ａ以外の他の流動層には空気（Ｏ2 ＝２１％）が注気さ
れているので、排ガス再循環風箱域より拡散してきた、
一部ガス化した廃棄物が効率よく燃焼する。これは、流
動床特有の欠点である廃棄物投入量変化、質変化に対し
て、フレキシブルに対応できることを意味しており、従
来のように、被処理物のドカ落ち（大量に落下するこ
と）によるＣＯの異常発生（例えば、瞬時１０００ppm
）を防止することができる。As described above, when the exhaust gas for recirculation of exhaust gas is used in the small air box in the area for introducing the material to be treated, the oxygen concentration for combustion in this portion is reduced from 21% to approximately 10%, so that the flow in this portion is reduced. The burning rate in the bed is reduced, the quality of the waste,
It becomes easier to absorb load fluctuations in the amount of waste. Further, since air (O 2 = 21%) is injected into the fluidized bed other than zone A, it has diffused from the exhaust gas recirculation wind box area.
The partially gasified waste efficiently burns. This means that it is possible to flexibly respond to changes in the amount of waste input and changes in quality that are the peculiarities of the fluidized bed. Abnormal occurrence of CO due to
) Can be prevented.
【００１６】また、被処理物投入域（ゾーンＡ）の流動
層温度が６００℃近辺にあると、安定燃焼が可能であ
り、そのため、最も重要な廃棄物投入域の温度を検出し
て、排ガス再循環量を制御（流動層の流動化条件から、
最大（Ｈ）、最小（Ｌ）の流量を設定）する。これです
べて制御できない場合には、前述のように補助制御とし
て、別途この部分に注水制御を行なう。なお、上記の制
御方法以外に、循環する排ガス量を一定に制御する方法
を採用することもある。本実施例では、通常の流動床炉
について説明したが、流動媒体を２室間で循環させる循
環流動床炉にも本発明を適用することが可能である。Further, when the temperature of the fluidized bed in the material input area (zone A) is around 600 ° C., stable combustion is possible, and therefore the temperature of the most important waste material input area is detected to detect the exhaust gas. Controlling the amount of recirculation (from the fluidization conditions of the fluidized bed,
Set the maximum (H) and minimum (L) flow rates). If all cannot be controlled by this, water injection control is separately performed on this portion as auxiliary control as described above. In addition to the above control method, a method of controlling the circulating exhaust gas amount to a constant value may be adopted. Although a normal fluidized bed furnace has been described in the present embodiment, the present invention can also be applied to a circulating fluidized bed furnace in which a fluid medium is circulated between two chambers.
【００１７】[0017]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 （１） 注水量を低減することができるので、炉内温度
の低下を防ぐことができ、完全燃焼及び安定燃焼を図る
ことができる。 （２） 注水量を低減することができるので、水の潜熱
分、熱ロスがなくなって熱効率の向上につながり、ガス
冷却装置がボイラ方式の場合は、発生蒸気量を増すこと
ができる。 （３） 流動層内のＯ2 濃度は排ガス再循環分下げられ
るが、流動用気体のトータル流量が変わらないため、不
燃物排出特性は変わらず、良好な効果が得られる。な
お、不燃物排出性能は流動用空気量と大きく関係するた
め、風箱へ供給する全風量は変えることができない。Since the present invention is configured as described above, it has the following effects. (1) Since the amount of injected water can be reduced, the temperature inside the furnace can be prevented from lowering, and complete combustion and stable combustion can be achieved. (2) Since the amount of injected water can be reduced, the latent heat of water and heat loss are eliminated, leading to an improvement in thermal efficiency. When the gas cooling device is a boiler system, the amount of generated steam can be increased. (3) The O 2 concentration in the fluidized bed can be reduced by the amount of exhaust gas recirculation, but the total flow rate of the fluidizing gas does not change, so the incombustible emission characteristics do not change, and good effects can be obtained. Since the incombustible discharge performance is largely related to the flow air volume, the total air volume supplied to the air box cannot be changed.
【図１】本発明の流動床炉における安定燃焼方法を実施
する装置の一実施例を示すフローシートである。FIG. 1 is a flow sheet showing an example of an apparatus for carrying out a stable combustion method in a fluidized bed furnace of the present invention.
【図２】図１におけるII矢視図である。FIG. 2 is a view on arrow II in FIG.
【図３】本発明の方法を実施する装置の他の実施例を示
すフローシートである。FIG. 3 is a flow sheet showing another embodiment of the apparatus for carrying out the method of the present invention.
【図４】図３におけるIV矢視図である。FIG. 4 is a view on arrow IV in FIG.
【図５】本発明の方法を実施する装置のさらに他の実施
例を示すフローシートである。FIG. 5 is a flow sheet showing still another embodiment of the apparatus for carrying out the method of the present invention.
【図６】従来の流動床炉における安定燃焼方法を実施す
る装置のフローシートである。FIG. 6 is a flow sheet of an apparatus for performing a stable combustion method in a conventional fluidized bed furnace.
１０ 流動床炉 １２ 流動層 １４ 温度制御手段 １６ 空気押込ファン １８ 不燃物排出導管 ２０ 注水ライン ２２ 水量調節弁 ２４ 小風箱 ２４ａ 小風箱 ２６ 空気分散板 ２８ 風箱 ３０ 排ガス再循環ライン ３２ 排ガス流量調節手段 ３４ 被処理物投入口 ３６ 仕切板 ３８ ガス冷却装置 ４０ 排ガス処理装置 ４２ 誘引ファン ４４ 排ガス再循環用ファン ４６ 煙突 ５０ 排ガス流量検出制御手段 Ａ 被処理物投入ゾーン Ｂ 他のゾーン 10 fluidized bed furnace 12 fluidized bed 14 temperature control means 16 air pushing fan 18 incombustibles discharge conduit 20 water injection line 22 water quantity control valve 24 small wind box 24a small wind box 26 air dispersion plate 28 wind box 30 exhaust gas recirculation line 32 exhaust gas flow rate Control means 34 Processing object input port 36 Partition plate 38 Gas cooling device 40 Exhaust gas treatment device 42 Induction fan 44 Exhaust gas recirculation fan 46 Chimney 50 Exhaust gas flow rate detection control means A Processing object input zone B Other zones
Claims (5)
下側の風箱に、熱回収後の冷却された燃焼排ガスを循環
・供給し、風箱の他の部分には空気を供給して流動媒体
を流動化させることを特徴とする流動床炉における安定
燃焼方法。1. A cooled combustion exhaust gas after heat recovery is circulated and supplied to a wind box below a fluidized bed of a treatment object input zone of a fluidized bed furnace, and air is supplied to other parts of the wind box. A stable combustion method in a fluidized bed furnace, characterized in that the fluidized medium is fluidized.
入ゾーンの流動層温度を制御することを特徴とする請求
項１記載の流動床炉における安定燃焼方法。2. The stable combustion method in a fluidized bed furnace according to claim 1, wherein the amount of combustion exhaust gas supplied is adjusted to control the temperature of the fluidized bed in the zone for introducing the material to be treated.
限を設けることを特徴とする請求項２記載の流動床炉に
おける安定燃焼方法。3. The stable combustion method in a fluidized bed furnace according to claim 2, wherein maximum and minimum limits are set for controlling the flue gas flow rate.
炉の被処理物投入ゾーンの流動層下側に小風箱を設け、
この小風箱に熱回収後の冷却された燃焼排ガスを循環・
供給するための、排ガス流量調節手段を備えた排ガス再
循環ラインを接続し、流動層に接続された温度制御手段
と前記排ガス流量調節手段とを、排ガス流量により流動
層温度を制御するように接続したことを特徴とする流動
床炉における安定燃焼装置。4. A small wind box is provided below the fluidized bed in a treatment object charging zone of a fluidized bed furnace having a fluidized bed fluidized with air.
Circulate the cooled combustion exhaust gas after heat recovery in this small wind box
An exhaust gas recirculation line equipped with an exhaust gas flow rate adjusting means for supply is connected, and a temperature control means connected to the fluidized bed and the exhaust gas flow rate adjusting means are connected so as to control the fluidized bed temperature by the exhaust gas flow rate. A stable combustion apparatus in a fluidized bed furnace characterized by the above.
流動層に接続されていることを特徴とする請求項４記載
の流動床炉における安定燃焼装置。5. The stable combustion apparatus in a fluidized bed furnace according to claim 4, wherein the temperature control means is connected to the fluidized bed of the processing object charging zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6078199A JP2681748B2 (en) | 1994-03-23 | 1994-03-23 | Stable combustion method and apparatus in fluidized bed furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6078199A JP2681748B2 (en) | 1994-03-23 | 1994-03-23 | Stable combustion method and apparatus in fluidized bed furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07260122A true JPH07260122A (en) | 1995-10-13 |
| JP2681748B2 JP2681748B2 (en) | 1997-11-26 |
Family
ID=13655348
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6078199A Expired - Lifetime JP2681748B2 (en) | 1994-03-23 | 1994-03-23 | Stable combustion method and apparatus in fluidized bed furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2681748B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105889909A (en) * | 2016-05-31 | 2016-08-24 | 中国华能集团清洁能源技术研究院有限公司 | Large fluidized bed boiler blending combustion system |
| CN105928186A (en) * | 2016-05-03 | 2016-09-07 | 长沙恒宇节能环保科技有限公司 | Efficient waste heat boiler |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05196202A (en) * | 1992-01-20 | 1993-08-06 | Ishikawajima Harima Heavy Ind Co Ltd | Fluidized bed boiler |
-
1994
- 1994-03-23 JP JP6078199A patent/JP2681748B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05196202A (en) * | 1992-01-20 | 1993-08-06 | Ishikawajima Harima Heavy Ind Co Ltd | Fluidized bed boiler |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105928186A (en) * | 2016-05-03 | 2016-09-07 | 长沙恒宇节能环保科技有限公司 | Efficient waste heat boiler |
| CN105889909A (en) * | 2016-05-31 | 2016-08-24 | 中国华能集团清洁能源技术研究院有限公司 | Large fluidized bed boiler blending combustion system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2681748B2 (en) | 1997-11-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4938170A (en) | Thermal reactor | |
| JPH0610526B2 (en) | Fluidized bed combustion method and apparatus | |
| JPS62169921A (en) | Stable combustion of fluidized bed furnace | |
| EP1213534B1 (en) | Combustion method in which generation of NOx, CO and dioxine are suppressed and fluidized bed incinerator therefor | |
| JPS5843312A (en) | Load controlling for fluidized bed boiler | |
| JP2681748B2 (en) | Stable combustion method and apparatus in fluidized bed furnace | |
| JPH06323510A (en) | Combustion control method in fluidized bed type furnace | |
| JP3913229B2 (en) | Circulating fluid furnace | |
| EP0237712A1 (en) | Method of combustion for fluidized bed incinerators | |
| JP3247066B2 (en) | Freeboard temperature control method for fluidized bed incinerator. | |
| JPH07198111A (en) | Combustor inside temperature control method for circulating fluidized bed boiler | |
| JP2971421B2 (en) | Combustion control method for fluidized bed incinerator | |
| JP2941785B1 (en) | Operating method of fluidized bed incinerator and its incinerator | |
| KR20150014490A (en) | Circulating-type multi-layer furnace | |
| JP6916974B1 (en) | Fluidized bed processing furnace | |
| JP2623404B2 (en) | Operating method and apparatus of fluidized bed incinerator | |
| JP3030016B2 (en) | Operating method of fluidized bed incinerator and its incinerator | |
| JP2937737B2 (en) | Fluidized bed combustion method and apparatus with partial combustion | |
| JPH10220722A (en) | Method of avoiding coating in partial combustion furnace | |
| JP2729915B2 (en) | Fluidized bed furnace cooling method | |
| JP2000121025A (en) | Method for controlling combustion of fluidized bed incinerator | |
| JPH064172Y2 (en) | Reactor pressure control device for fluidized bed combustor | |
| JP2686343B2 (en) | Circulating fluidized bed combustor control method | |
| JPH1114029A (en) | Circulating fluidized bed combustion equipment and method of operation | |
| JPH06281108A (en) | Method for mixed combustion of low calorific value gas/in circulation fludized bed type boiler |