JPH0225624A - Temperature control of cyclone coal combustion furnace - Google Patents

Temperature control of cyclone coal combustion furnace

Info

Publication number
JPH0225624A
JPH0225624A JP63176549A JP17654988A JPH0225624A JP H0225624 A JPH0225624 A JP H0225624A JP 63176549 A JP63176549 A JP 63176549A JP 17654988 A JP17654988 A JP 17654988A JP H0225624 A JPH0225624 A JP H0225624A
Authority
JP
Japan
Prior art keywords
combustion
air
furnace
cyclone
cyclone body
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
JP63176549A
Other languages
Japanese (ja)
Other versions
JP2616808B2 (en
Inventor
Michihiro Shiraha
白羽 陸宏
Kenichi Fujii
健一 藤井
Shingo Suzutani
鈴谷 信吾
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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
Application filed by Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP63176549A priority Critical patent/JP2616808B2/en
Publication of JPH0225624A publication Critical patent/JPH0225624A/en
Application granted granted Critical
Publication of JP2616808B2 publication Critical patent/JP2616808B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Coke Industry (AREA)
  • Regulation And Control Of Combustion (AREA)
  • Air Supply (AREA)

Abstract

PURPOSE:To make it possible to control the temperature of the furnace wall even during the operation under a low load by utilizing air used for secondary combustion and air used for two-stage combustion for cooling the body of a furnace and at the same time controlling the amount of circulation of cooling air while the temperature of the furnace wall is sensed. CONSTITUTION:After the main body 2 of a cyclone is cooled by supplying combustion air to a cooling air flow channel 18 which is between the inner plate 16 and outer plate 17 of the main body 2 of the cyclone, the combustion air is used as secondary air and two-stage combustion air. And part of exhaust gas from the combustion of a secondary furnace is used with the combustion air for cooling the main body 2 of the cyclone by circulating the exhaust gas and combustion air, and the temperature of the inner plate 16 is sensed and the opening and closing of a damper 28 or a valve in a line 27 of the circulating air are made after the main body 2 of the cyclone is cooled in order to regulate the volume of the circulating air sent to a cooling gas flow channel 18. Namely, the volume of the circulating air is regulated by the damper 28 or the valve in order to prevent an excessive rise in the temperature of the inner plate 16. And, the surface temperature of a refractory material 32 which is lined on the inner plate 16 is sensed and a damper 34 or a valve of a circulation line 25 of the exhaust gas from the combustion is controlled by its opening or closing.

Description

【発明の詳細な説明】 (産業上の利用分野〕 本発明は、ボイラ火炉などの工業炉を炉本体とし、この
炉本体の前炉として微粉炭、微粉オイルコークス、スラ
ッジなどの固体燃料(以下、単に石炭という)を燃焼用
旋回空気により燃焼させるサイクロン石炭燃焼炉の耐火
材および内洞板などの内板を保護するための温度制御方
法に関するものである。
Detailed Description of the Invention (Industrial Field of Application) The present invention uses an industrial furnace such as a boiler furnace as a furnace body, and uses solid fuel such as pulverized coal, pulverized oil coke, or sludge (hereinafter referred to as The present invention relates to a temperature control method for protecting inner plates such as refractory materials and inner cavity plates of a cyclone coal combustion furnace in which coal (simply referred to as coal) is combusted by swirling air for combustion.

〔従来の技術〕[Conventional technology]

従来から、ボイラ火炉などの工業炉においては、炉本体
に前炉(−火炉)としてサイクロン石炭燃焼炉を設けて
石炭を部分燃焼させるようにしたものが知られている。
BACKGROUND ART Conventionally, industrial furnaces such as boiler furnaces are known in which a cyclone coal combustion furnace is provided as a front furnace (-furnace) in the furnace body to partially burn coal.

このような前炉を備えた工業炉(二次炉)は、燃焼効果
が優れたものであることから、広く用いられている。
Industrial furnaces (secondary furnaces) equipped with such forehearths are widely used because of their excellent combustion effects.

上記の従来型のサイクロン石炭燃焼炉の構造を示すもの
として、たとえば先に捉案した実開昭607671.7
号公報に示されるように、微粉炭と空気とをサイクロン
石炭燃焼炉内に供給するとともに、これらを高速旋回流
として効果的に混合して燃焼させることにより、微粉炭
を部分燃焼させる構造のものが開示されている。すなわ
ち、第4図に示すように、ボイラ火炉などの火炉(二次
炉)1の側壁にサイクロン本体2を横方向に取り付け、
このサイクロン本体に石炭投入口3、燃焼用旋回空気供
給口4および燃焼ガスを火炉へ導くガス導通口5を設け
、サイクロン本体2の内部に、この本体2内で発生する
燃焼ガスを通過させ溶融スラグをせき止めるためのスラ
グパンフルロを設けるとともに、スラグパンフルの燃焼
ガス上流側に下向きのスラグ流下ロアを設けたサイクロ
ン石炭燃焼炉8が記載されている。10はスラグタンク
、11は燃焼室、12はバイパスライン、13は火炎で
ある。
As an illustration of the structure of the above-mentioned conventional cyclone coal combustion furnace, for example, the previously proposed Utility Model No. 607671.7
As shown in the publication, a structure in which pulverized coal is partially combusted by supplying pulverized coal and air into a cyclone coal combustion furnace and effectively mixing and burning them as a high-speed swirling flow. is disclosed. That is, as shown in FIG. 4, the cyclone main body 2 is attached laterally to the side wall of a furnace (secondary furnace) 1 such as a boiler furnace,
The cyclone body is provided with a coal input port 3, a swirling air supply port 4 for combustion, and a gas communication port 5 for guiding combustion gas to the furnace, and the combustion gas generated within the main body 2 is passed through the cyclone body 2 to melt it. A cyclone coal combustion furnace 8 is described that is provided with a slag pan fluro for damming up slag, and a downward slag flow lower is provided on the combustion gas upstream side of the slag pan flue. 10 is a slag tank, 11 is a combustion chamber, 12 is a bypass line, and 13 is a flame.

また1967年ニELSEVIERPUBLISIII
NG COMPANY (オランダ国)から発行された
“’LARGE ROIIJRFullNACES″に
は、サイクロン石炭燃焼炉の内板と外板との間に空気を
通して炉を冷却する方法および装置が記載されている。
Also in 1967
"'LARGE ROII JRFullNACES", published by NG COMPANY (Netherlands), describes a method and apparatus for cooling a cyclone coal-fired furnace by passing air between its inner and outer plates.

さらに燃焼炉に燃焼排ガス循環う・インを設けて、燃焼
排ガスを循環させることで、燃焼温度および耐火材温度
を制御する方法も、従来から知られている。
Furthermore, a method of controlling combustion temperature and refractory material temperature by providing a combustion furnace with a combustion exhaust gas circulation inlet and circulating the combustion exhaust gas has also been known.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記の第4図に示すサイクロン石炭燃焼炉においては、
サイクロン本体周囲の耐火材および内鋼板を保護するた
めに、これらを冷却する必要がある。
In the cyclone coal combustion furnace shown in Figure 4 above,
In order to protect the fireproof materials and inner steel plates around the cyclone body, it is necessary to cool them.

また上記のオランダ文献に記載されたサイクロン石炭燃
焼炉においては、低負荷運転時の冷却媒体量が確保でき
ないために、内洞板温度が過度に上昇し損傷するなどの
不都合点がある。
Further, in the cyclone coal combustion furnace described in the above-mentioned Dutch document, since the amount of cooling medium cannot be secured during low-load operation, there are disadvantages such as an excessive rise in the temperature of the inner cavity plate and damage.

さらに上記の燃焼排ガス循環ラインを設ける方式では、
循環排ガス量を増やすと、耐火材表面温度および内洞板
温度が低下するものの、低負荷運転時には耐火材表面温
度が低下しすぎて燃焼トラブルを起こすおそれがある。
Furthermore, in the method of installing the combustion exhaust gas circulation line mentioned above,
If the amount of circulating exhaust gas is increased, the surface temperature of the refractory material and the temperature of the inner cavity plate will decrease; however, during low load operation, the surface temperature of the refractory material may drop too much and cause combustion troubles.

なおサイクロン石炭燃焼炉では、スラグの溶融流動性確
保の制約のため、耐火材表面温度の適正範囲はきわめて
狭い。
In addition, in a cyclone coal combustion furnace, the appropriate range of refractory material surface temperature is extremely narrow due to restrictions on ensuring the melt fluidity of slag.

本発明は上記の諸点に鑑みなされたもので、空冷式のサ
イクロン石炭燃焼炉において、炉内壁を構成する耐火材
およびメタル面の両者を広い運転負荷にわたって保護す
るために、二次燃焼用空気および二段燃焼用空気のいず
れをも炉体冷却用空気として利用し、低負荷運転時にお
ける炉体冷却空気量の低下を防止するため炉体冷却空気
循環ラインを設けて、炉壁の温度を検知しつつ冷却空気
循環量を制御することにより、低負荷運転時でも炉壁温
度を制御することができる方法を提供することを目的と
するものである。
The present invention was made in view of the above points, and is designed to protect both the refractory material and the metal surface that make up the inner wall of the furnace over a wide range of operating loads in an air-cooled cyclone coal combustion furnace. Both of the two-stage combustion air is used as furnace cooling air, and in order to prevent the amount of furnace cooling air from decreasing during low-load operation, a furnace cooling air circulation line is installed to detect the temperature of the furnace wall. It is an object of the present invention to provide a method that can control the furnace wall temperature even during low-load operation by controlling the amount of circulating cooling air.

〔問題点を解決するための手段および作用〕上記の目的
を達成するために、本発明のサイクロン石炭燃焼炉にお
ける温度制御方法は、図面に示すように、二次炉1の側
壁にサイクロン本体2を横方向に取り付け、このサイク
ロン本体に石炭投入口3、燃焼用旋回空気供給口4、燃
焼ガスを二次炉へ導くガス導通口5およびスラグ流下ロ
アを設けたサイクロン石炭燃焼炉8において、燃焼空気
をサイクロン本体2の内板16と外板17との間の冷却
気体流路18に供給してサイクロン本体2を冷却した後
、二次空気および二段燃焼空気として使用し、さらに二
次炉の燃焼排ガスの一部を前記燃焼空気とともにサイク
ロン本体2の冷却に循環使用し、内板16温度を検知し
て、サイクロン本体2を冷却した後の循環空気のライン
27のダンパ28または弁を開閉制御して、冷却気体流
路18へ送る循環空気量を調節することを特徴としてい
る。すなわち、内板16温度の過上昇防止のために、循
環空気量をダンパ28または弁で調整する。
[Means and operations for solving the problems] In order to achieve the above object, the temperature control method in a cyclone coal combustion furnace of the present invention includes a cyclone main body 2 on the side wall of the secondary furnace 1, as shown in the drawings. is attached laterally, and the cyclone coal combustion furnace 8 is equipped with a coal input port 3, a swirling air supply port 4 for combustion, a gas communication port 5 for guiding combustion gas to the secondary furnace, and a slag flow lower lower in the cyclone body. After cooling the cyclone body 2 by supplying air to the cooling gas passage 18 between the inner plate 16 and outer plate 17 of the cyclone body 2, the air is used as secondary air and second-stage combustion air, and is then used as secondary air and second-stage combustion air. A part of the combustion exhaust gas is circulated together with the combustion air to cool the cyclone body 2, and the temperature of the inner plate 16 is detected to open and close the damper 28 or valve of the circulating air line 27 after cooling the cyclone body 2. It is characterized by controlling and adjusting the amount of circulating air sent to the cooling gas flow path 18. That is, in order to prevent the temperature of the inner plate 16 from rising excessively, the amount of circulating air is adjusted using the damper 28 or the valve.

また本発明の方法は、燃焼空気をサイクロン本体2の内
板16と外板17との間の冷却気体流路18に供給して
サイクロン本体2を冷却した後、二次空気および二段燃
焼空気として使用し、さらに二次炉の燃焼排ガスの一部
を前記燃焼空気とともにサイクロン本体2の冷却に循環
使用し、内板16に内張りされた耐火材32の表面温度
を検知して、燃焼排ガス循環ライン25のダンパ34ま
たは弁を開閉制御することを特徴としている。すなわち
、耐火材32表面温度の制御のために、循環排ガス量を
ダンパ34または弁で調整する。なお、燃焼排ガスライ
ン24は、ボイラ出口から煙突入口のどの部分から取り
出してもよい。
Furthermore, the method of the present invention cools the cyclone body 2 by supplying combustion air to the cooling gas passage 18 between the inner plate 16 and the outer plate 17 of the cyclone body 2, and then supplies the secondary air and the second stage combustion air. Furthermore, a part of the combustion exhaust gas from the secondary furnace is circulated together with the combustion air to cool the cyclone body 2, and the surface temperature of the refractory material 32 lined with the inner plate 16 is detected, and the combustion exhaust gas is circulated. It is characterized by controlling the opening and closing of the damper 34 or valve of the line 25. That is, in order to control the surface temperature of the refractory material 32, the amount of circulating exhaust gas is adjusted using the damper 34 or the valve. Note that the combustion exhaust gas line 24 may be taken out from any part of the smoke inlet from the boiler outlet.

〔実 施 例〕〔Example〕

以下、図面を参照して本発明の好適な実施例を詳細に説
明する。ただしこの実施例に記載されている構成機器の
材質、形状、その相対配置などは、とくに特定的な記載
がない限りは、本発明の範囲をそれらのみに限定する趣
旨のものではなく、単なる説明例にすぎない。
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. However, unless there is a specific description, the materials, shapes, relative positions, etc. of the components described in this example are not intended to limit the scope of the present invention to these, but are merely illustrative. Just an example.

第1図は本発明のサイクロン石炭燃焼炉における温度制
御方法を実施する装置の一例を示している。燃焼空気を
押込ファン14により空気予熱器15に送入し、ここで
加熱した後、加熱された燃焼空気をサイクロン本体2の
内網板などの内板16と外鋼板などの外板17との間の
冷却気体流路18に供給して、サイクロン本体2を冷却
する。
FIG. 1 shows an example of an apparatus for implementing the temperature control method in a cyclone coal combustion furnace of the present invention. Combustion air is sent to an air preheater 15 by a forced fan 14 and heated there, and then the heated combustion air is passed between an inner plate 16 such as an inner mesh plate of the cyclone body 2 and an outer plate 17 such as an outer steel plate. The cyclone body 2 is cooled by being supplied to the cooling gas flow path 18 between the two.

冷却気体流路18を出た空気は、二次空気および二段燃
焼空気として使用される。20は二次空気ライン、21
は二段燃焼空気ラインである。
The air exiting the cooling gas flow path 18 is used as secondary air and second stage combustion air. 20 is a secondary air line, 21
is a two-stage combustion air line.

またボイラ火炉などの二次炉1の燃焼排ガスの一部を前
記燃焼空気とともに、サイクロン本体2の冷却に循環使
用し、燃焼排ガスの残部は前記空気予熱器15、誘引フ
ァン22を経て煙突23から排出される。24は燃焼排
ガスライン、25ば燃焼排ガス循環ラインである。
Also, a part of the combustion exhaust gas from the secondary furnace 1 such as a boiler furnace is circulated and used together with the combustion air for cooling the cyclone body 2, and the remaining combustion exhaust gas passes through the air preheater 15 and the induction fan 22, and then flows out from the chimney 23. It is discharged. 24 is a combustion exhaust gas line, and 25 is a combustion exhaust gas circulation line.

そして内板16の温度を温度検出器26で検知して、サ
イクロン本体2を冷却した後の循環空気が流れる空気循
環ライン27のダンパ28を開閉制御して、冷却気体流
路18へ送る循環空気量を調節する。30は制御装置、
31は循環ファンである。
Then, the temperature of the inner plate 16 is detected by the temperature detector 26, and the damper 28 of the air circulation line 27 through which the circulating air after cooling the cyclone body 2 flows is controlled to open and close, and the circulating air is sent to the cooling gas flow path 18. Adjust the amount. 30 is a control device;
31 is a circulation fan.

温度検出器2乙の検知温度(内板の温度)が高すぎると
、ダンパ28を開いて循環空気量を多くするように制御
する。
If the temperature detected by the temperature detector 2B (temperature of the inner plate) is too high, the damper 28 is opened to increase the amount of circulating air.

また内板16には耐火材32が内張すされており、この
耐火材32の表面温度を温度検出器33で検知して、燃
焼排ガス循環ライン25のダンパ34を開閉制御する。
The inner plate 16 is lined with a refractory material 32, and the surface temperature of the refractory material 32 is detected by a temperature detector 33 to control the opening and closing of the damper 34 of the combustion exhaust gas circulation line 25.

35は制御装置である。35 is a control device.

温度検出器33の検知温度が高いと、ダンパ34を開い
て燃焼排ガス循環量を多くして、耐火材32表面温度を
低くするように制御する。
When the temperature detected by the temperature detector 33 is high, the damper 34 is opened to increase the circulation amount of the combustion exhaust gas, thereby controlling the surface temperature of the refractory material 32 to be lowered.

なお−例として各部の温度を挙げると、空気予熱器15
出口の空気温度は200’C前後、冷却気体流路18の
出口の空気温度は600℃前後、二次炉1の出口の燃焼
排ガス温度は300”C前後である。また第1図におい
て、(a)は二次空気量、(b)は二段燃焼空気量、F
C)は冷却後の循環空気量、(d)は循環燃焼排ガス量
を示している。
In addition, to take the temperature of each part as an example, the air preheater 15
The air temperature at the outlet is around 200'C, the air temperature at the outlet of the cooling gas flow path 18 is around 600'C, and the combustion exhaust gas temperature at the outlet of the secondary furnace 1 is around 300'C. a) is the secondary air amount, (b) is the second stage combustion air amount, F
C) shows the amount of circulating air after cooling, and (d) shows the amount of circulating combustion exhaust gas.

第2図は、サイクロン石炭燃焼炉内の各部の温度と燃焼
負荷との関係を実測した結果を示している。第2図にお
いて、実線は従来の循環なしの場合の実測値を示し、破
線は空気循環と燃焼排ガス循環とを含む本発明の方法を
実施した場合の実測値を示している。
FIG. 2 shows the results of actually measuring the relationship between the temperature of each part in the cyclone coal combustion furnace and the combustion load. In FIG. 2, the solid line shows the measured value in the conventional case without circulation, and the broken line shows the measured value in the case of implementing the method of the present invention including air circulation and combustion exhaust gas circulation.

第3図は、本発明の方法を実施した場合の各空気量およ
び循環燃焼排ガス量の実測例を示している。
FIG. 3 shows an example of actual measurement of each amount of air and amount of circulating combustion exhaust gas when the method of the present invention is implemented.

なお(a)〜(ロ)は第1図に示すものと同じである。Note that (a) to (b) are the same as shown in FIG.

〔発明の効果〕〔Effect of the invention〕

本発明は上記のように構成されているので、耐火材、内
網板などの温度制御をすることができ、このためこれら
の温度の過上昇による材料損傷を防止することができる
という効果を有している。
Since the present invention is configured as described above, it is possible to control the temperature of the refractory material, inner mesh plate, etc., and therefore, it has the effect of being able to prevent damage to the materials due to excessive rise in temperature. are doing.

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

第1図は本発明のサイクロン石炭燃焼炉における温度制
御方法を実施する装置の一例を示す説明図、第2図は燃
焼負荷と各部の温度との関係を示す線図、第3図は燃焼
負荷と循環気体流量との関係を示す線図、第4図は従来
のサイクロン石炭燃焼炉の一例を示す断面図である。 1・・・火炉(二次炉)、2・・・サイクロン本体、3
・・・石炭投入口、4・・・燃焼用旋回空気供給口、5
・・・ガス導通口、6・・・スラグバッフル、7・・・
スラグ流下口、8・・・サイクロン石炭燃焼炉、10・
・・スラグタ7り、11・・・燃焼室、12・・・バイ
パスライン、13・・・火炎、14・・・押込ファン、
15・・・空気予熱器、16・・・内板、17・・・外
板、I8・・・冷却気体流路、20・・・二次空気ライ
ン、21・・・二段燃焼空気ライン、22・・・誘引フ
ァン、23・・・煙突、24・・・燃焼排ガスライン、
25・・・燃焼排ガス循環ライン、26・・・温度検出
器、27・・・空気循環ライン、28・・・ダンパ、3
0・・・制御装置、31・・・循環ファン、32・・・
耐火材、33・・・温度検出器、34・・・ダンパ、3
5−・・制イ1装置
Fig. 1 is an explanatory diagram showing an example of a device implementing the temperature control method in a cyclone coal combustion furnace of the present invention, Fig. 2 is a diagram showing the relationship between combustion load and temperature of each part, and Fig. 3 is a combustion load FIG. 4 is a sectional view showing an example of a conventional cyclone coal combustion furnace. 1... Furnace (secondary furnace), 2... Cyclone body, 3
... Coal input port, 4... Combustion swirling air supply port, 5
...Gas communication port, 6...Slag baffle, 7...
Slag outlet, 8...Cyclone coal combustion furnace, 10.
... Slagta 7ri, 11 ... Combustion chamber, 12 ... Bypass line, 13 ... Flame, 14 ... Forced fan,
15... Air preheater, 16... Inner plate, 17... Outer plate, I8... Cooling gas flow path, 20... Secondary air line, 21... Two-stage combustion air line, 22... Induction fan, 23... Chimney, 24... Combustion exhaust gas line,
25... Combustion exhaust gas circulation line, 26... Temperature detector, 27... Air circulation line, 28... Damper, 3
0...Control device, 31...Circulation fan, 32...
Fireproof material, 33... Temperature detector, 34... Damper, 3
5-... Control 1 device

Claims (1)

【特許請求の範囲】 1 二次炉の側壁にサイクロン本体を横方向に取り付け
、このサイクロン本体に石炭投入口、燃焼用旋回空気供
給口、燃焼ガスを二次炉へ導くガス導通口およびスラグ
流下口を設けたサイクロン石炭燃焼炉において、燃焼空
気をサイクロン本体の内板と外板との間の冷却気体流路
に供給してサイクロン本体を冷却した後、二次空気およ
び二段燃焼空気として使用し、さらに二次炉の燃焼排ガ
スの一部を前記燃焼空気とともにサイクロン本体の冷却
に循環使用し、内板温度を検知して、サイクロン本体を
冷却した後の循環空気のラインのダンパまたは弁を開閉
制御して、冷却気体流路へ送る循環空気量を調節するこ
とを特徴とするサイクロン石炭燃焼炉における温度制御
方法。 2 二次炉の側壁にサイクロン本体を横方向に取り付け
、このサイクロン本体に石炭投入口、燃焼用旋回空気供
給口、燃焼ガスを二次炉へ導くガス導通口およびスラグ
流下口を設けたサイクロン石炭燃焼炉において、燃焼空
気をサイクロン本体の内板と外板との間の冷却気体流路
に供給してサイクロン本体を冷却した後、二次空気およ
び二段燃焼空気として使用し、さらに二次炉の燃焼排ガ
スの一部を前記燃焼空気とともにサイクロン本体の冷却
に循環使用し、内板に内張りされた耐火材の表面温度を
検知して、燃焼排ガス循環ラインのダンパまたは弁を開
閉制御することを特徴とするサイクロン石炭燃焼炉にお
ける温度制御方法。
[Scope of Claims] 1. A cyclone body is installed horizontally on the side wall of the secondary furnace, and the cyclone body has a coal input port, a swirling air supply port for combustion, a gas communication port for guiding combustion gas to the secondary furnace, and a slag flow downstream. In a cyclone coal-burning furnace equipped with a port, combustion air is supplied to the cooling gas flow path between the inner and outer plates of the cyclone body to cool the cyclone body, and then used as secondary air and second-stage combustion air. Furthermore, part of the combustion exhaust gas from the secondary furnace is circulated together with the combustion air to cool the cyclone body, and the internal plate temperature is detected and a damper or valve in the circulating air line after cooling the cyclone body is activated. A temperature control method in a cyclone coal combustion furnace, characterized by controlling opening and closing to adjust the amount of circulating air sent to a cooling gas flow path. 2. A cyclone coal system in which a cyclone body is installed horizontally on the side wall of the secondary furnace, and the cyclone body is provided with a coal input port, a swirling air supply port for combustion, a gas communication port for guiding combustion gas to the secondary furnace, and a slag flow port. In the combustion furnace, combustion air is supplied to the cooling gas flow path between the inner plate and the outer plate of the cyclone body to cool the cyclone body, and then used as secondary air and second stage combustion air, and is then used as secondary air and second stage combustion air. A part of the combustion exhaust gas is circulated together with the combustion air to cool the cyclone body, and the surface temperature of the refractory material lined on the inner plate is detected to control the opening and closing of dampers or valves in the combustion exhaust gas circulation line. Characteristics of temperature control method in cyclone coal combustion furnace.
JP63176549A 1988-07-15 1988-07-15 Temperature control method in cyclone coal combustion furnace Expired - Lifetime JP2616808B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63176549A JP2616808B2 (en) 1988-07-15 1988-07-15 Temperature control method in cyclone coal combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63176549A JP2616808B2 (en) 1988-07-15 1988-07-15 Temperature control method in cyclone coal combustion furnace

Publications (2)

Publication Number Publication Date
JPH0225624A true JPH0225624A (en) 1990-01-29
JP2616808B2 JP2616808B2 (en) 1997-06-04

Family

ID=16015527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63176549A Expired - Lifetime JP2616808B2 (en) 1988-07-15 1988-07-15 Temperature control method in cyclone coal combustion furnace

Country Status (1)

Country Link
JP (1) JP2616808B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5174143A (en) * 1991-11-05 1992-12-29 Mcdonnell Douglas Corporation Surface densification of porous materials
CN102588951A (en) * 2012-03-21 2012-07-18 德清县华恒涂装设备有限公司 Biomass burner
KR101228420B1 (en) * 2012-06-18 2013-01-31 (주)유성 Dividing air of combustion chamber having cooling equipment
JP2014013093A (en) * 2012-07-03 2014-01-23 Takuma Co Ltd Method for controlling air-cooled wall surface temperature for combustion furnace, and combustion furnace using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5174143A (en) * 1991-11-05 1992-12-29 Mcdonnell Douglas Corporation Surface densification of porous materials
CN102588951A (en) * 2012-03-21 2012-07-18 德清县华恒涂装设备有限公司 Biomass burner
KR101228420B1 (en) * 2012-06-18 2013-01-31 (주)유성 Dividing air of combustion chamber having cooling equipment
JP2014013093A (en) * 2012-07-03 2014-01-23 Takuma Co Ltd Method for controlling air-cooled wall surface temperature for combustion furnace, and combustion furnace using the same

Also Published As

Publication number Publication date
JP2616808B2 (en) 1997-06-04

Similar Documents

Publication Publication Date Title
US4592293A (en) Method of controlling an air heater of a coal-fired boiler
CN209978093U (en) System for controlling temperature of boiler burner of coal-fired power plant to avoid burning loss
KR20030019364A (en) Waste incinerator and method of operating the incinerator
CN113108308A (en) Method for adjusting wall temperature of flash combustion boiler after low-load abrasion stop
CN110906359B (en) Combustion device capable of adjusting secondary air temperature and using method
JPH0225624A (en) Temperature control of cyclone coal combustion furnace
JPH036404B2 (en)
JP2003262317A (en) Combustion air supply amount adjustment device for combustible gas combustion chamber
TW202424390A (en) Combustion equipment
JP2000028129A (en) Pulverized coal combustor
US5730070A (en) Apparatus for introducing gas recirculation to control steam temperature in steam generation systems
JPS6127410A (en) Combustion apparatus
JP2692876B2 (en) NOx control device for incinerator
US3310096A (en) Apparatus for securing burners
JP2008032345A (en) Combustion melting furnace and operation method of combustion melting furnace
JPH035613A (en) Incinerator
SU1200109A1 (en) Method of regulating furnace temperature
JPS5682314A (en) Sludge incinerator
SK277956B6 (en) Heating method of fluid layer by given of fluid focus into working and fluid combusting device for realization of this method
JPH0552529U (en) Fluidized bed waste incinerator temperature controller
JPH1061929A (en) Control method for supplying secondary combustion air in combustion device
JPS59164815A (en) Control of fire grate temperature
JPH04214118A (en) Continuous heating furnace and controller of combustion switching
GB1059345A (en) Improvements in or relating to incinerators
RU1788021C (en) Method for heating regenerator with high-calorific fuel