JPH01111122A - Cyclone coal combustion furnace system recovering sensible heat of slag - Google Patents

Cyclone coal combustion furnace system recovering sensible heat of slag

Info

Publication number
JPH01111122A
JPH01111122A JP62266244A JP26624487A JPH01111122A JP H01111122 A JPH01111122 A JP H01111122A JP 62266244 A JP62266244 A JP 62266244A JP 26624487 A JP26624487 A JP 26624487A JP H01111122 A JPH01111122 A JP H01111122A
Authority
JP
Japan
Prior art keywords
slag
air
cooling
cyclone
coal combustion
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
JP62266244A
Other languages
Japanese (ja)
Other versions
JPH0756381B2 (en
Inventor
Shingo Suzutani
鈴谷 信吾
Shunpei Nozoe
野添 浚平
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 JP62266244A priority Critical patent/JPH0756381B2/en
Publication of JPH01111122A publication Critical patent/JPH01111122A/en
Publication of JPH0756381B2 publication Critical patent/JPH0756381B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

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  • Air Supply (AREA)

Abstract

PURPOSE:To recover sensible heat of slag and increase an efficiency of a boiler plant by a method wherein the slag under its molten condition of high temperature which is discharged from a cyclone coal furnace is cooled by air and cooling air of which temperature is increased through heat exchanging operation is used as combustion air for fine powder coal. CONSTITUTION:Fine powder coal is ignited within a cyclone coal furnace 1, ashes contained in the fine powder coal are dropped onto a cooling floor 3 of slag within a slag heat exchanging chamber 17. Cooled air fed from a cooling air blower 9 cools molten metal of high temperature. The cooled slag is crushed by a crusher 4 and sent onto a discharging conveyor 6. Cooling air of high temperature is fed into a cyclone separator 8 to separate fine slags, discharges them onto the discharging conveyor 5 located at a lower part. Clean hot air is fed into a suction side of a fine powder coal combustion forced blower 10. The blower 10 may suck hot air and surrounding atmosphere, heat exchange with discharged gas of a boiler 2 by a gas air preheater 12, further increase its temperature and the air is fed into a furnace 1 and acts as combustion air for fine powder coal injected from feeding hole.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は送入された微粉炭を高温・高熱負荷の条件下で
燃焼し、周壁に付着させた燃焼灰を溶融状態にて排出す
るサイクロン石炭燃焼炉を真数したボイラに関するもの
である。
[Detailed description of the invention] [Industrial application field] The present invention is a cyclone that burns introduced pulverized coal under conditions of high temperature and high heat load, and discharges the combustion ash attached to the peripheral wall in a molten state. This relates to a boiler that is the antithesis of a coal-fired furnace.

[従来の技術] ボイラ本体燃焼室に付設し、送入孔から噴出した微粉炭
を高温・高熱負荷の条件下て燃焼し、周壁に付着させた
燃焼灰を溶融状態にて排出し、高温の可燃性燃焼ガスを
ボイラ本体燃焼室に送入するサイクロン石炭燃焼炉方式
においては、サイクロン石炭燃焼炉から排出したスラグ
はダクトを経て内部に水を満たした水封装置中に落下さ
せることにより、急激な冷却によるスラグの粗粒化と冷
却を行ない、冷却された粗粒状のスラグをコンペヤによ
って排出し、スラグコンテナに送入していた。この方式
はスラグの冷却に水を使用することにより、冷却が短時
間に行なわれること、冷却源が水であるために冷却に要
する運転コストが低いこと、冷却設備の建設費が低いこ
と、冷却設備がコンパクトになること等の他に、高温の
スラグを水の中に投入し急速に冷却することによりスラ
グが粗粒状に破砕されると言う利点を有していた。
[Conventional technology] The pulverized coal attached to the combustion chamber of the boiler main body is blown out from the inlet hole under conditions of high temperature and high heat load, and the combustion ash adhering to the surrounding wall is discharged in a molten state. In the cyclone coal-fired furnace system, in which combustible combustion gas is sent into the combustion chamber of the boiler main body, the slag discharged from the cyclone coal-fired furnace is dropped through a duct into a water-sealing device filled with water. The slag was coarsened and cooled by cooling, and the cooled coarse slag was discharged by a conveyor and sent to a slag container. This method uses water to cool the slag, so cooling can be done in a short time, the operating cost required for cooling is low because the cooling source is water, the construction cost of cooling equipment is low, and the cooling In addition to making the equipment more compact, this method had the advantage of crushing the slag into coarse particles by pouring the high-temperature slag into water and cooling it rapidly.

[発明が解決しようとする問題点] しかしながら上記従来のサイクロン石炭燃焼炉方式にお
いては、生成される多量のスラグなすべて水中に投入し
冷却することにより、高温のスラグの有する顕熱はすべ
て冷却水の蒸発温熱として消費されることにより、多量
の熱量の損失を招くと言う不都合を有していた。
[Problems to be Solved by the Invention] However, in the conventional cyclone coal combustion furnace system described above, all the generated slag is poured into water and cooled, so that all the sensible heat of the high temperature slag is absorbed by the cooling water. This has the disadvantage that a large amount of heat is lost because it is consumed as evaporation heat.

[問題点を解決するための手段] 上記問題点を解決するための手段は、前記特許請求の範
囲に記載のとおり、サイクロン石炭燃焼炉を有するボイ
ラにおいて、サイクロン石炭燃焼炉のスラグ排出孔の下
流側に熱交換室を設け、該熱交換室にはスラグを一時滞
留する手段と、スラグ冷却用空気導入手段と、サイクロ
ン石炭燃焼炉の燃焼用空気吸入口に連通ずる高温空気排
出手段を設けたスラグの顕熱を回収するサイクロン石炭
燃焼炉システムである。
[Means for Solving the Problems] As described in the claims, the means for solving the problems described above are provided in a boiler having a cyclone coal-fired furnace, in a boiler downstream of a slag discharge hole of the cyclone coal-fired furnace. A heat exchange chamber was provided on the side, and the heat exchange chamber was provided with means for temporarily retaining slag, means for introducing air for cooling the slag, and means for discharging high temperature air that communicated with the combustion air inlet of the cyclone coal combustion furnace. This is a cyclone coal combustion furnace system that recovers sensible heat from slag.

[作 用] まずボイラ本体があり、ボイラ本体の燃焼室にはサイク
ロン石炭燃焼炉が真数されている。サイクロン石炭燃焼
炉のスラグ排出孔の下流側にスラグ熱交換室がある。熱
交換室にはスラグを一時滞留する手段が内設されており
、スラグ冷却用空気の導入手段および高温空気排出手段
が接続されている。高温空気排出手段を構成する出口ダ
クトは、必要によりサイクロンセパレータ、微粉炭燃焼
用押込送風機、ガス空気予熱器などを経由してサイクロ
ン石炭燃焼炉に至っている。サイクロン石炭燃焼炉で生
成された溶融状態のスラグは、スラグ排出孔から熱交換
室に落下する。熱交換室でスラグと熱交換を行ない温度
の上昇した冷却空気は必要に応じてサイクロンセパレー
タに入り、微細スラグを分離して下部のスラグ排出コン
ベヤ上に排出するなどして清浄化され、微粉炭燃焼用押
込送風機の吸込側に送入される。微粉炭燃焼用押込送風
機は、このようにして得られた高温空気と大気とを吸引
し、ガス空気予熱器によってボイラ排ガスと熱交換を行
ない、更に温度を上昇させたのち、サイクロン石炭燃焼
炉に送入され、送入孔から噴出した微粉炭の燃焼用空気
として作用する。したがって本発明によれば、サイクロ
ン石炭燃焼炉から排出された高温の溶融状態のスラグな
空気によって冷却し、その際熱交換によって昇温した空
気をサイクロン石炭燃焼炉における微粉炭の燃焼用空気
として使用することにより、スラグ顕熱の回収を行なう
ことが可能になると言う効果を有する。
[Function] First, there is the boiler body, and the combustion chamber of the boiler body has a cyclone coal combustion furnace. There is a slag heat exchange chamber downstream of the slag discharge hole of the cyclone coal combustion furnace. The heat exchange chamber has a means for temporarily retaining the slag, and is connected to a means for introducing air for cooling the slag and a means for discharging high-temperature air. The outlet duct constituting the high-temperature air discharge means leads to the cyclone coal combustion furnace via a cyclone separator, a forced air blower for pulverized coal combustion, a gas air preheater, etc., as necessary. The molten slag produced in the cyclone coal combustion furnace falls into the heat exchange chamber from the slag discharge hole. The cooled air, whose temperature has increased by exchanging heat with the slag in the heat exchange chamber, enters the cyclone separator as necessary, where it is purified by separating fine slag and discharging it onto the slag discharge conveyor at the bottom. It is sent to the suction side of the forced air blower for combustion. The forced air blower for pulverized coal combustion sucks the high-temperature air and atmosphere obtained in this way, exchanges heat with the boiler exhaust gas using a gas air preheater, further raises the temperature, and then transfers it to the cyclone coal combustion furnace. It acts as combustion air for the pulverized coal that is introduced and ejected from the inlet hole. Therefore, according to the present invention, the air is cooled by the high temperature molten slag air discharged from the cyclone coal combustion furnace, and the air heated by heat exchange is used as combustion air for pulverized coal in the cyclone coal combustion furnace. This has the effect of making it possible to recover the sensible heat of the slag.

[実施例] 以下に本発明の実施例を図面に基いて説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例を示すスラグの顕熱を回収す
るサイクロン石炭燃焼炉システムの系統図である。第1
図において、1はサイクロン石炭燃焼炉、2はボイラ本
体、3はスラグな一時滞留させるスラグ冷却床、4はク
ラッシャ、5はスラグ排出コンベヤ、6はスラグバンカ
、7はスラグ冷却空気出口ダクト、8はサイクロンセパ
レータ、9はスラグ冷却空気送風機、10は微粉炭燃焼
用押込送風機、11は微粉炭燃焼用押込送風機吐出側ダ
クト、12はガス空気予熱器、13は圧力調節器、14
は風量調整ダンパ、15は誘引通風機、16は煙突、1
7はスラグ熱交換室、18はボイラ排ガスダクト、19
はスラグ冷却空気入口ダクトである。サイクロン石炭燃
焼炉1において、送入孔から噴出した微粉炭は高温・高
熱負荷の条件下で燃焼し、微粉炭中の灰分は燃焼ガスの
旋回力によって周壁に衝突し、付着したのち溶融状態で
スラグ排出孔から排出し、下部に配設したスラグ熱交換
室17のスラグ冷却床3上に落下する。スラグ冷却床3
の上部からはスラグ冷却空気送風機9から送入された冷
空気が吹きつけられ高温の溶融スラグを冷却する。スラ
グ冷却床3の内部にはスラグ冷却空気出口ダクト7が内
設されており、スラグ冷却床3上のスラグを冷却し、熱
交換して高温となった冷却空気を吸引している。スラグ
冷却床3上で冷却されたスラグはスラグ冷却床3の端部
からクラッシャ4上に落下し破砕されて粗粒状となり、
下部のスラグ排出コンベヤ5上に送られる。スラグ排出
コンベヤ5に送られた粗粒状スラグは更にスラグバンカ
6に送られ貯蔵される。スラグ冷却床3の内部で吸引さ
れた高温の冷却空気は一部の微細スラグを浮遊させた状
態でサイクロンセパレータ8に送入され、微細スラグを
分離して下部のスラグ排出コンベヤ5上に排出し、清浄
な高温空気は微粉炭燃焼用押込送風機10の吸込側に送
入される。微粉炭燃焼用押込送風機10はサイクロンセ
パレータ8から送入された高温空気と大気とを吸引し、
ガス空気予熱器12によってボイラ2の排ガスと熱交換
を行ない、更に温度を上昇させたのちサイクロン石炭燃
焼炉1に送入され、送入孔から噴出した微粉炭の燃焼用
空気として作用する。スラグ冷却空気送風機9の出口ダ
クトには風量調整ダンパ14が配設されており、サイク
ロン石炭燃焼炉1の炉内圧力とスラグ熱交換室17の内
部圧力とをバランスさせており、これによってスラグ冷
却空気送風機9から送入される冷却用空気がスラグ排出
孔からサイクロン石炭燃焼炉1内に浸入して過剰空気と
なるのを防止するとともに、スラグ熱交換室17への送
入冷却風量の不足によってスラグの冷却不十分な状態を
生じ、スラグ冷却床3の閉塞或いはクラッシャ4への溶
着等の生じるのを防止している。
FIG. 1 is a system diagram of a cyclone coal combustion furnace system for recovering sensible heat from slag, showing one embodiment of the present invention. 1st
In the figure, 1 is a cyclone coal combustion furnace, 2 is a boiler body, 3 is a slag cooling bed for temporarily retaining slag, 4 is a crusher, 5 is a slag discharge conveyor, 6 is a slag bunker, 7 is a slag cooling air outlet duct, and 8 is a slag cooling air outlet duct. Cyclone separator, 9 is a slag cooling air blower, 10 is a forced air blower for pulverized coal combustion, 11 is a duct on the discharge side of the forced air blower for pulverized coal combustion, 12 is a gas air preheater, 13 is a pressure regulator, 14
is an air volume adjustment damper, 15 is an induced draft fan, 16 is a chimney, 1
7 is a slag heat exchange chamber, 18 is a boiler exhaust gas duct, 19
is the slag cooling air inlet duct. In the cyclone coal combustion furnace 1, the pulverized coal ejected from the inlet is burned under conditions of high temperature and high heat load, and the ash in the pulverized coal collides with the surrounding wall due to the swirling force of the combustion gas, adheres to it, and then becomes molten. The slag is discharged from the slag discharge hole and falls onto the slag cooling bed 3 of the slag heat exchange chamber 17 provided at the bottom. Slag cooling bed 3
Cold air is blown from the top of the slag cooling air blower 9 to cool the high temperature molten slag. A slag cooling air outlet duct 7 is installed inside the slag cooling bed 3 to cool the slag on the slag cooling bed 3 and suck in the cooling air that has become hot through heat exchange. The slag cooled on the slag cooling bed 3 falls from the end of the slag cooling bed 3 onto the crusher 4 and is crushed into coarse particles.
The slag is sent onto the lower slag discharge conveyor 5. The coarse slag sent to the slag discharge conveyor 5 is further sent to a slag bunker 6 and stored therein. The high-temperature cooling air sucked inside the slag cooling bed 3 is sent to the cyclone separator 8 with some fine slag suspended, and the fine slag is separated and discharged onto the slag discharge conveyor 5 at the bottom. The clean high-temperature air is introduced into the suction side of the forced air blower 10 for pulverized coal combustion. The forced air blower 10 for pulverized coal combustion sucks the high-temperature air sent in from the cyclone separator 8 and the atmosphere,
After exchanging heat with the exhaust gas of the boiler 2 by the gas-air preheater 12 and further raising the temperature, the air is fed into the cyclone coal combustion furnace 1 and acts as combustion air for the pulverized coal ejected from the feed hole. An air volume adjustment damper 14 is disposed at the outlet duct of the slag cooling air blower 9, and balances the pressure inside the cyclone coal combustion furnace 1 with the internal pressure of the slag heat exchange chamber 17, thereby cooling the slag. This prevents the cooling air sent from the air blower 9 from entering the cyclone coal combustion furnace 1 through the slag discharge hole and becoming excess air, and also prevents the cooling air from flowing into the slag heat exchange chamber 17 from insufficient cooling air volume. This prevents the slag from being insufficiently cooled, resulting in clogging of the slag cooling bed 3 or welding to the crusher 4.

第2〜4図は本発明の他の実施例を示すもので、第2図
は全体系統図、第3図はスラグ熱交換室の構造図、第4
図は振動型スラグ冷却床の構造図である。説明を簡単に
するために第2〜4図において第1図と同様の作用をな
す部分は第1図と同一符号で説明する。第2〜4図にお
いて3は振動型スラグ冷却床、20は加振器、21はス
ラグ冷却床冷却水人口管、22はスラグ冷却床冷却水出
口管、23はスラグ粉砕粒子落下孔、24は冷却空気孔
である。サイクロン石炭燃焼炉1において、送入孔から
噴出した微粉炭は高温・高熱負荷の条件下で燃焼し、微
粉炭中の灰分は燃焼ガスの旋回力によって周壁に衝突し
、付着したのち溶融状態でスラグ排出孔から排出し、下
部に配設したスラグ熱交換室17中に落下する。落下し
たスラグは、スラグ冷却空気送風機9から送入された冷
空気によって塊状で冷却され凝固する。凝固したスラグ
はクラッシャ4にて粗粉砕され、下部のスラグ冷却床3
上に至る。スラグ冷却床3は水冷構造の多孔板によって
形成されており、上下方向に複数個構設され、いずれも
加振器20によって振動が与えられる。またスラグ冷却
床3にはスラグ粉砕粒子落下孔23および冷却空気孔2
4が穿設されており、スラグ粉砕粒子の上方から下方へ
の落下およびスラグ冷却空気の下方から上方への通過が
可能な構造になっている。これによってスラグ冷却床3
上に落下した粗粉砕されたスラグは、低温の冷却床への
接触と下方から送入される低温のスラグ冷却空気によっ
て更に冷却されるとともに、振動する多孔板によって更
に細粒に粉砕されたのち、スラグ熱交換室17の下部に
配設されたスラグ排出コンベヤ5上に落下する。スラグ
排出コンベヤ5上に落下した細粒状のスラグはスラグバ
ンカ6に送られ貯蔵される。スラグ熱交換室17内のク
ラッシャ4の上部およびスラグ冷却床3においてスラグ
を冷却し、熱交換して高温となったスラグ冷却空気は、
微細スラグを浮遊させた状態でスラグ冷却空気出口ダク
ト7を経てサイクロンセパレータ8に送入され、微細ス
ラグを分離して下部のスラグ排出コンベヤ5上に排出し
、清浄な高温空気は微粉炭燃焼用押込送風機10の吸込
側に送入される。微粉炭燃焼用押込送風機10はサイク
ロンセパレータ8から送入された高温空気と大気とを吸
引し、ガス空気予熱器12によってボイラ2の排ガスと
熱交換を行ない、更に温度を上昇させたのちサイクロン
石炭燃焼炉1に送入され、送入孔から噴出した微粉炭の
燃焼用空気として作用する。スラグ冷却用送風機9の出
口ダクトには風量調整ダンパ14が配設されており、サ
イクロン石炭燃焼炉1の炉内圧力とスラグ熱交換室17
の内部圧力とをバランスさせており、これによってスラ
グ冷却空気送風機9から送入される冷却用空気がスラグ
排出孔からサイクロン石炭燃焼炉1内に浸入して過剰空
気となるのを防止するとともに、スラグ熱交換室17へ
の送入冷却風量の不足によってスラグの冷却不十分な状
態を生じ、スラグ冷却床3の閉塞或いはクラッシャ4へ
の溶着等の生じるのを防止している。
Figures 2 to 4 show other embodiments of the present invention, where Figure 2 is an overall system diagram, Figure 3 is a structural diagram of a slag heat exchange chamber, and Figure 4 is a structural diagram of a slag heat exchange chamber.
The figure is a structural diagram of a vibrating slag cooling bed. In order to simplify the explanation, parts in FIGS. 2 to 4 that have the same functions as in FIG. 1 are designated by the same reference numerals as in FIG. 1. In Figures 2 to 4, 3 is a vibrating slag cooling bed, 20 is an exciter, 21 is a slag cooling bed cooling water artificial pipe, 22 is a slag cooling bed cooling water outlet pipe, 23 is a slag pulverized particle falling hole, and 24 is a It is a cooling air hole. In the cyclone coal combustion furnace 1, the pulverized coal ejected from the inlet is burned under conditions of high temperature and high heat load, and the ash in the pulverized coal collides with the surrounding wall due to the swirling force of the combustion gas, adheres to it, and then becomes molten. The slag is discharged from the slag discharge hole and falls into the slag heat exchange chamber 17 provided at the bottom. The fallen slag is cooled and solidified in a lump by the cold air sent from the slag cooling air blower 9. The solidified slag is coarsely crushed by a crusher 4, and then sent to a lower slag cooling bed 3.
reach the top. The slag cooling bed 3 is formed of a perforated plate having a water-cooled structure, and a plurality of slag cooling beds 3 are provided in the vertical direction, and each of them is given vibration by the vibrator 20. In addition, the slag cooling bed 3 includes slag pulverized particle drop holes 23 and cooling air holes 2.
4 is perforated, and has a structure that allows slag crushed particles to fall from above to below and slag cooling air to pass from below to above. As a result, the slag cooling bed 3
The coarsely crushed slag that has fallen to the top is further cooled by contact with the low-temperature cooling bed and the low-temperature slag-cooling air sent in from below, and is further crushed into fine particles by a vibrating perforated plate. , and fall onto the slag discharge conveyor 5 disposed at the bottom of the slag heat exchange chamber 17. The fine-grained slag that has fallen onto the slag discharge conveyor 5 is sent to a slag bunker 6 and stored. The slag is cooled in the upper part of the crusher 4 and the slag cooling bed 3 in the slag heat exchange chamber 17, and the slag cooling air which has become high temperature through heat exchange,
The suspended fine slag is sent to the cyclone separator 8 through the slag cooling air outlet duct 7, where the fine slag is separated and discharged onto the lower slag discharge conveyor 5, and the clean high temperature air is used for pulverized coal combustion. The air is fed into the suction side of the forced air blower 10. The forced air blower 10 for pulverized coal combustion sucks the high temperature air and atmosphere sent in from the cyclone separator 8, exchanges heat with the exhaust gas of the boiler 2 through the gas air preheater 12, further raises the temperature, and then converts it into cyclone coal. The air is fed into the combustion furnace 1 and acts as combustion air for the pulverized coal ejected from the feed hole. An air volume adjustment damper 14 is disposed at the outlet duct of the slag cooling blower 9, and the slag heat exchange chamber 17 changes the pressure inside the cyclone coal combustion furnace 1.
This prevents the cooling air sent from the slag cooling air blower 9 from entering the cyclone coal combustion furnace 1 from the slag discharge hole and becoming excess air. This prevents the slag from being insufficiently cooled due to an insufficient amount of cooling air sent to the slag heat exchange chamber 17, and from clogging the slag cooling bed 3 or welding to the crusher 4.

[発明の効果コ 本発明は上記実施例から明らかなように、サイクロン石
炭燃焼炉を具設したボイラにおいて、サイクロン石炭燃
焼炉から排出された高温の溶融状態のスラグな空気によ
って冷却し、その際熱交換を行なって昇温した冷却用空
気をサイクロン石炭燃焼炉における微粉炭の燃焼用空気
として使用することによってスラグの顕熱を回収し、サ
イクロン石炭燃焼炉を具設したボイラのプラント効率を
上昇させることが可能になると言う効果を有する。
[Effects of the Invention] As is clear from the above embodiments, the present invention provides a boiler equipped with a cyclone coal combustion furnace, in which cooling is performed by high temperature molten slag air discharged from the cyclone coal combustion furnace. By using the cooling air heated through heat exchange as combustion air for pulverized coal in a cyclone coal combustion furnace, the sensible heat of the slag is recovered and the plant efficiency of a boiler equipped with a cyclone coal combustion furnace is increased. This has the effect of making it possible to

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

第1〜4図は本発明に基くスラグの顕熱を回収するサイ
クロン石炭燃焼炉システムの例で、第1図はスラグ冷却
床にコンベヤ型を使用した場合の全体系統図、第2図は
スラグ冷却床に振動型を使用した場合の全体系統図、第
3図は第2図におけるスラグ熱交換室の構造図、第4図
は第2〜3図における振動型スラグ冷却床の構造図であ
る。 1・・・サイクロン石炭燃焼炉、2・・・ボイラ本体、
3・・・スラグ冷却床、     4・・・クラッシャ
、5・・・スラグ排出コンベヤ、6・・・スラグバンカ
、7・・・スラグ冷却空気出口ダクト、 8・・・サイクロンセパレータ、 9・・・スラグ冷却空気送風機、 10・・・微粉炭燃焼用押込送風機、 11・・・微粉炭燃焼用押込送風機吐出側ダクト、12
・・・ガス空気予熱器、   13・・・圧力調節器、
14・・・風量調整ダンパ、 15・・・誘引通風機、
16・・・煙突、      17・・・スラグ熱交換
室、18・・・ボイラ排ガスダクト、 19・・・スラグ冷却空気入口ダクト、20・・・加振
器、 21・・・スラグ冷却床冷却水入口管、22・・・スラ
グ冷却床冷却水出口管、23・・・スラグ粉砕粒子落下
孔、 24・・・冷却空気孔。
Figures 1 to 4 are examples of a cyclone coal combustion furnace system for recovering sensible heat from slag based on the present invention. Figure 1 is an overall system diagram when a conveyor type is used for the slag cooling bed, and Figure 2 is a slag Figure 3 is a structural diagram of the slag heat exchange chamber in Figure 2, and Figure 4 is a structural diagram of the vibrating slag cooling bed in Figures 2 and 3. . 1... Cyclone coal combustion furnace, 2... Boiler body,
3... Slag cooling bed, 4... Crusher, 5... Slag discharge conveyor, 6... Slag bunker, 7... Slag cooling air outlet duct, 8... Cyclone separator, 9... Slag Cooling air blower, 10... Forced air blower for pulverized coal combustion, 11... Forced air blower discharge side duct for pulverized coal combustion, 12
...Gas air preheater, 13...Pressure regulator,
14... Air volume adjustment damper, 15... Induced draft fan,
16... Chimney, 17... Slag heat exchange chamber, 18... Boiler exhaust gas duct, 19... Slag cooling air inlet duct, 20... Exciter, 21... Slag cooling bed cooling water Inlet pipe, 22...Slag cooling bed cooling water outlet pipe, 23...Slag crushed particle fall hole, 24...Cooling air hole.

Claims (3)

【特許請求の範囲】[Claims] (1)サイクロン石炭燃焼炉を有するボイラにおいて、
サイクロン石炭燃焼炉のスラグ排出孔の下流側に熱交換
室を設け、該熱交換室にはスラグを一時滞留する手段と
、スラグ冷却用空気導入手段と、サイクロン石炭燃焼炉
の燃焼用空気吸入口に連通する高温空気排出手段を設け
たことを特徴とするスラグの顕熱を回収するサイクロン
石炭燃焼炉システム。
(1) In a boiler with a cyclone coal combustion furnace,
A heat exchange chamber is provided downstream of the slag discharge hole of the cyclone coal combustion furnace, and the heat exchange chamber includes a means for temporarily retaining slag, an air introduction means for cooling the slag, and a combustion air intake port of the cyclone coal combustion furnace. A cyclone coal combustion furnace system for recovering sensible heat from slag, characterized by having a high temperature air exhaust means communicating with the slag.
(2)スラグを一時滞留する手段がスラグ排出コンベヤ
である特許請求の範囲第(1)項記載のスラグの顕熱を
回収するサイクロン石炭燃焼炉システム。
(2) A cyclone coal combustion furnace system for recovering sensible heat from slag according to claim (1), wherein the means for temporarily retaining slag is a slag discharge conveyor.
(3)スラグを一時滞留する手段が振動可能な多孔板で
ある特許請求の範囲第(1)項記載のスラグの顕熱を回
収するサイクロン石炭燃焼炉システム。
(3) A cyclone coal combustion furnace system for recovering sensible heat from slag according to claim (1), wherein the means for temporarily retaining slag is a vibrating perforated plate.
JP62266244A 1987-10-23 1987-10-23 Cyclone coal combustion furnace system to recover sensible heat of slag Expired - Lifetime JPH0756381B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62266244A JPH0756381B2 (en) 1987-10-23 1987-10-23 Cyclone coal combustion furnace system to recover sensible heat of slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62266244A JPH0756381B2 (en) 1987-10-23 1987-10-23 Cyclone coal combustion furnace system to recover sensible heat of slag

Publications (2)

Publication Number Publication Date
JPH01111122A true JPH01111122A (en) 1989-04-27
JPH0756381B2 JPH0756381B2 (en) 1995-06-14

Family

ID=17428277

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62266244A Expired - Lifetime JPH0756381B2 (en) 1987-10-23 1987-10-23 Cyclone coal combustion furnace system to recover sensible heat of slag

Country Status (1)

Country Link
JP (1) JPH0756381B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997000406A1 (en) * 1995-06-19 1997-01-03 Magaldi Ricerche E Brevetti S.R.L. Conveyor/cooler of loose materials

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5946415A (en) * 1982-08-26 1984-03-15 Nippon Furnace Kogyo Kaisha Ltd Primary air feeder for rotary kiln

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5946415A (en) * 1982-08-26 1984-03-15 Nippon Furnace Kogyo Kaisha Ltd Primary air feeder for rotary kiln

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997000406A1 (en) * 1995-06-19 1997-01-03 Magaldi Ricerche E Brevetti S.R.L. Conveyor/cooler of loose materials

Also Published As

Publication number Publication date
JPH0756381B2 (en) 1995-06-14

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