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JPH0143231B2 - - Google Patents
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JPH0143231B2 - - Google Patents

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Publication number
JPH0143231B2
JPH0143231B2 JP17213483A JP17213483A JPH0143231B2 JP H0143231 B2 JPH0143231 B2 JP H0143231B2 JP 17213483 A JP17213483 A JP 17213483A JP 17213483 A JP17213483 A JP 17213483A JP H0143231 B2 JPH0143231 B2 JP H0143231B2
Authority
JP
Japan
Prior art keywords
furnace
firing
combustion chamber
inner cylinder
truncated conical
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
Application number
JP17213483A
Other languages
Japanese (ja)
Other versions
JPS6064179A (en
Inventor
Masamitsu Ootsuka
Hiroshi Masuda
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP17213483A priority Critical patent/JPS6064179A/en
Publication of JPS6064179A publication Critical patent/JPS6064179A/en
Publication of JPH0143231B2 publication Critical patent/JPH0143231B2/ja
Granted legal-status Critical Current

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  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 この発明は焼成炉に関し、特に石灰石などの細
粒材を焼成するための二重傾斜型焼成炉に係るも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a firing furnace, and more particularly to a double inclined firing furnace for firing fine grain materials such as limestone.

〔従来技術〕[Prior art]

従来例によるこの種の焼成炉は、上下方向断面
が非対称形状で、水平方向断面が長方形状に構成
されており、その構造上ならびに操炉上におい
て、次のような不利があつた。すなわち、上下方
向断面が不安定な非対称形状であつて、自立可能
な安定構造物でないために、転倒防止用の大規模
な架構とか、各部分への補強部材を必要としてい
て、多量の鋼材を使用しなければならず、そのた
めの材料費ならびに加工組立て費が必要であり、
また水平方向断面が長方形状であるために、断面
積当りに対する所要煉瓦数が多くなるだけでな
く、両サイドに壁面が形成されて、ガスならびに
原石の流れに速度差を生ずる。すなわち、炉内の
壁面に接した部分ではガスが吹抜け、かつ原石の
流下速度が大きくなつて、中央部分ではガスの流
れが悪く、原石の流下速度が小さくなつて、結果
的に焼成むらを生ずることになる。さらに構造上
から長辺方向の大きさを長くできず、ひいては大
型化にも限界があつた。
Conventional firing furnaces of this type have an asymmetric cross section in the vertical direction and a rectangular cross section in the horizontal direction, and have the following disadvantages in terms of structure and furnace operation. In other words, since it has an asymmetrical shape with an unstable vertical cross section and is not a stable structure that can stand on its own, it requires a large-scale structure to prevent falls and reinforcing members for each part, which requires a large amount of steel. material costs and processing and assembly costs are required.
Furthermore, since the horizontal cross section is rectangular, not only does the number of bricks required per cross-sectional area increase, but also walls are formed on both sides, creating a speed difference in the flow of gas and raw stone. In other words, gas blows through in the area that is in contact with the wall of the furnace, and the falling speed of the rough stone increases, while in the central area, the gas flow is poor and the falling speed of the rough stone decreases, resulting in uneven firing. It turns out. Furthermore, due to the structure, it was not possible to increase the size in the long side direction, and there was a limit to increasing the size.

〔発明の概要〕[Summary of the invention]

この発明は従来の焼成炉のこのような欠点に鑑
み、円筒状内筒に形成した円錐台状部と、この内
筒周囲に被嵌状態で設けられる円筒状外筒の円錐
台対応部に形成した膨出部との組み合せにより、
複数の焼成帯を構成した炉体構造を基本とする焼
成炉を提供するものである。
In view of these drawbacks of conventional firing furnaces, the present invention has developed a truncated conical part formed in a cylindrical inner cylinder and a corresponding part formed in a truncated conical part of a cylindrical outer cylinder fitted around the inner cylinder. In combination with the bulge,
The present invention provides a firing furnace based on a furnace body structure comprising a plurality of firing zones.

〔発明の実施例〕[Embodiments of the invention]

以下、この発明に係る焼成炉の一実施例につ
き、添付図面を参照して詳細に説明する。
Hereinafter, one embodiment of the firing furnace according to the present invention will be described in detail with reference to the accompanying drawings.

添付図面において、横断面円筒状の内筒1は、
上下方向中間部に円錐台状部2を周方向に突出形
成させて基礎架台3上に保持されていて、その円
錐台状部2から下方の内部には、周囲に冷却通路
4を介して熱風煙道5を設けると共に、この煙道
5の下部を基礎架台3の下方に延長して熱風発生
炉6に接続させ、上部を円錐台状部2の下側に形
成される下部燃焼室7に向け複数箇所で開口させ
てあり、かつ円錐台状部2の上部周囲開口からは
内部に排気煙道8を形成して、この排気煙道8お
よび冷却通路4を上端側方のダクト9および10
に取り出してある。
In the accompanying drawings, the inner cylinder 1 having a cylindrical cross section is
A truncated conical part 2 is formed in the vertically intermediate part to protrude in the circumferential direction and is held on a base 3, and the interior below the truncated conical part 2 is supplied with hot air via a cooling passage 4 around the periphery. A flue 5 is provided, the lower part of the flue 5 is extended below the base frame 3 and connected to the hot air generating furnace 6, and the upper part is connected to the lower combustion chamber 7 formed under the truncated conical part 2. An exhaust flue 8 is formed inside from the opening around the upper part of the truncated conical part 2, and the exhaust flue 8 and the cooling passage 4 are connected to ducts 9 and 10 on the side of the upper end.
It has been taken out.

また前記内筒1の周囲に被嵌状態で設けられる
ところの、同様に横断面円筒状の外筒11は、前
記円錐台状部2に対応して同部2との間の上部に
上部燃焼室13、下部に前記下部燃焼室7を形成
するようにした膨出部12を周方向に形成させて
前記基礎架台3上に保持されており、その炉頂開
口部には、原石を受け入れるスカート状導入筒1
4と原石焼成後の排ガスを導出するダクト15と
を設け、上部燃焼室13の側方複数箇所に上部バ
ーナ16を配し、下方側部に循環ガス吸込口17
を取り出し、かつ底部には基礎架台3を通して製
品取り出し装置19に連通する取り出し開口18
を形成してある。
Further, an outer cylinder 11 having a cylindrical cross section and fitted around the inner cylinder 1 is provided with an upper combustion chamber in the upper part between the truncated conical part 2 and the truncated conical part 2. The chamber 13 is held on the base frame 3 with a bulge 12 formed in the circumferential direction to form the lower combustion chamber 7 at the bottom thereof, and a skirt for receiving raw ore is provided at the top opening of the furnace. Shape introduction tube 1
4 and a duct 15 for discharging the exhaust gas after firing the raw stone, upper burners 16 are arranged at multiple locations on the side of the upper combustion chamber 13, and a circulating gas suction port 17 is provided on the lower side.
There is a take-out opening 18 at the bottom which communicates with the product take-out device 19 through the base frame 3.
has been formed.

しかして、これらの内筒1および外筒11から
なる炉体構成の組み合せにより、炉内には上方か
ら、予熱帯A、上部焼成帯B、下部焼成帯C、並
流焼成帯D、製品冷却帯Eがそれぞれに構成され
る。
Therefore, due to the combination of the furnace structure consisting of the inner cylinder 1 and the outer cylinder 11, the furnace includes, from above, a preheating zone A, an upper firing zone B, a lower firing zone C, a cocurrent firing zone D, and a product cooling zone. Each band E is configured separately.

前記排気煙道8から取り出されたダクト9に
は、レキユペレータ20が接続されており、この
レキユペレータ20には1次作動空気ブロワ21
からの1次作動空気が給送され、こゝで熱交換さ
れた1次作動空気はヘツダ22を経て、一部の1
次空気が前記上部バーナ16に、他部の作動空気
が前記循環ガス吸込口17に接続させたインゼク
タ23にそれぞれ供給される。また、前記冷却通
路4には2次空気ブロワ24からの冷却空気を兼
ねる2次空気が給送され、冷却通路4を通つて熱
交換された2次空気は前記ダクト10からヘツダ
25を経て、一部が前記上部バーナ16に、他部
が前記熱風発生炉6にそれぞれ供給される。さら
に、前記製品取り出し装置19にダクト26から
吸引される3次空気を兼ねる冷却空気は、この装
置19ならびに取り出し開口18内の製品を冷却
しつゝ製品冷却帯Eを通つて熱交換され、前記循
環ガス吸込口17よりインゼクタ23、ヘツダ2
7を経て熱風発生炉6に至る。そして、この熱風
発生炉6および上部バーナ16には燃料ポンプ2
8から燃料が供給され、熱風発生炉6での燃焼で
得た高温の燃焼ガスは熱風煙道5を通つて前記下
部燃焼室7に吹き出され、その一部は並流焼成帯
Dに逆流して循環ガス吸込口17に達し、他部は
下部焼成帯Cを経たのち、上部バーナ16での高
温の燃焼ガスと共に上部焼成帯Bを通り、その一
部が前記排気煙道8、ダクト9からレキユペレー
タ20を経て、他部が予熱帯Aからダクト10を
経てそれぞれに排気ブロワ29に吸引され、この
排気ブロワ29から図示しない排気ガス集塵装置
を経て大気中に排出される。
A requiperator 20 is connected to the duct 9 taken out from the exhaust flue 8, and a primary operating air blower 21 is connected to the requiperator 20.
The primary working air from the
The secondary air is supplied to the upper burner 16, and the other working air is supplied to the injector 23 connected to the circulating gas suction port 17, respectively. Further, secondary air that also serves as cooling air from the secondary air blower 24 is supplied to the cooling passage 4, and the secondary air that has been heat exchanged through the cooling passage 4 passes from the duct 10 through the header 25. One part is supplied to the upper burner 16, and the other part is supplied to the hot air generating furnace 6. Further, the cooling air, which also serves as tertiary air, sucked into the product take-out device 19 from the duct 26 cools the product in the device 19 and the take-out opening 18, and is heat-exchanged through the product cooling zone E. Injector 23 and header 2 from circulating gas suction port 17
7 and then reaches a hot air generating furnace 6. A fuel pump 2 is connected to the hot air generating furnace 6 and the upper burner 16.
Fuel is supplied from 8, and the high-temperature combustion gas obtained by combustion in the hot air generating furnace 6 is blown out into the lower combustion chamber 7 through the hot air flue 5, and a part of it flows back into the cocurrent firing zone D. The other part passes through the lower firing zone C, and then passes through the upper firing zone B together with the high temperature combustion gas from the upper burner 16, and a part of it passes through the exhaust flue 8 and duct 9. After passing through the recuperator 20, the other parts are sucked into the exhaust blower 29 from the preheating zone A through the duct 10, and are discharged from the exhaust blower 29 into the atmosphere through an exhaust gas dust collector (not shown).

そして、また、前記炉頂の上方部には、原石搬
入コンベア30から給送される原石を受け入れる
ところの、断気用上部ダンパ32をもつサージホ
ツパ31と、このサージホツパ31から原石を切
り出す切り出しフイーダ33と、切り出される原
石を断気用下部ダンパ35から受け入れて前記ス
カート状導入筒14に均等投入する回転シユート
型の原石投入装置34と、原石投入レベルを測定
して投入制御を行なうサウジング装置36とを設
けてあり、さらに、前気製品排出装置19からの
製品を一旦受け入れる製品ホツパ37と、その断
気用排出ダンパ38と、製品ホツパ37からの製
品を集合する回転テーブル39と、製品搬出コン
ベア40とを設けたものである。
Further, in the upper part of the furnace top, there is a surge hopper 31 having an upper damper 32 for air isolation, which receives the rough stone fed from the rough stone carrying conveyor 30, and a cutting feeder 33 that cuts the rough stone from the surge hopper 31. , a rotary chute-type rough stone charging device 34 that accepts the raw stone to be cut from the lower damper 35 for air insulation and uniformly charges it into the skirt-shaped introduction tube 14, and a sounding device 36 that measures the raw stone input level and performs charging control. In addition, a product hopper 37 that once receives the product from the pre-air product discharge device 19, a discharge damper 38 for the air break, a rotary table 39 that collects the products from the product hopper 37, and a product discharge conveyor. 40.

この実施例の場合、搬入コンベア30によつて
給送される原石は、下部ダンパ35が閉じている
ときに開く上部ダンパ32部から、所期の一定量
づゝがサージホツパ31内に一旦貯溜され、この
サージホツパ31からは定期的に一定量の原石が
切り出しフイーダ33により切り出されて、下部
ダンパ35より原石投入装置34内に受け入れら
れ、かつ、同装置34の回転シユートにより炉頂
部のスカート状導入筒14内に均等に投入された
上で下部ダンパ35が閉じる。
In the case of this embodiment, a predetermined amount of raw ore fed by the carry-in conveyor 30 is temporarily stored in the surge hopper 31 from the upper damper 32 that opens when the lower damper 35 is closed. A certain amount of raw ore is periodically cut out from this surge hopper 31 by a cut feeder 33, received into the raw ore input device 34 from a lower damper 35, and introduced into a skirt shape at the top of the furnace by the rotating chute of the device 34. The lower damper 35 closes after it is evenly poured into the cylinder 14.

前記スカート状導入筒14から炉内を流下する
原石は、予熱帯Aにおいて燃焼排ガスにより予熱
されながら上部焼成帯Bに至る。そして、この上
部焼成帯Bにおいては、流下する原石の安息角に
より空間形成される上部燃焼室13での上部バー
ナ16からの燃焼ガスによつて焼成されながら、
円錐台状部2の外周傾斜面上を流下して下部焼成
帯Cに入る。またこの下部焼成帯Cにおいては、
同様に流下する原石の安息角により空間形成され
る下部燃焼室7で、熱風発生炉6から熱風煙道8
を経て吹き出される燃焼ガスにより再度焼成さ
れ、こゝでも膨出部12の内周下部傾斜面上を流
下して並流焼成帯Dに達する。こゝで、この並流
焼成帯Dにおいては、前記下部燃焼室7での燃焼
ガスの一部が後述するようにインゼクタ23に吸
引されて逆流し、こゝでの焼成がなされると共
に、製品冷却帯Eに至つてダクト26からの冷却
空気により冷却され、開口18を経て製品排出装
置19に受け入れられたのち、製品ホツパ37か
ら排出ダンパ38を通つて回転テーブル39で集
合されたのち、製品搬出コンベア40により外部
に取り出されるのである。
The raw ore flowing down through the furnace from the skirt-like introduction tube 14 reaches the upper firing zone B while being preheated by the combustion exhaust gas in the preheating zone A. In this upper firing zone B, the raw ore is fired by the combustion gas from the upper burner 16 in the upper combustion chamber 13, which is formed by the angle of repose of the falling raw ore.
It flows down on the outer peripheral inclined surface of the truncated conical part 2 and enters the lower firing zone C. Also, in this lower firing zone C,
Similarly, in the lower combustion chamber 7, a space is formed by the angle of repose of the falling rough stone, from the hot air generating furnace 6 to the hot air flue 8.
The fired gas is fired again by the combustion gas blown out through the bulging portion 12, and once again flows down on the sloped surface of the lower inner circumference of the bulging portion 12 to reach the parallel flow firing zone D. In this co-current firing zone D, part of the combustion gas in the lower combustion chamber 7 is sucked into the injector 23 and flows back, as will be described later, where the firing is performed and the product is After reaching the cooling zone E, the products are cooled by the cooling air from the duct 26, passed through the opening 18, and received by the product discharge device 19. After passing through the product hopper 37 and the discharge damper 38, the products are collected on the rotary table 39. It is taken out to the outside by a delivery conveyor 40.

しかして、この原石の焼成に際して、1次作動
空気ブロワ21からの1次作動空気は、レキユペ
レータ20により予熱されたのちに、その1次空
気はヘツダ22から前記上部バーナ16に供給さ
れて燃焼空気となり、その作動空気は同ヘツダ2
2からインゼクタ23に供給されて、前記ダクト
26からの3次空気、および前記下部燃焼室7か
ら逆流する燃焼ガスの吸引をなした上で、ヘツダ
27より前記熱風発生炉6に至つて燃焼される。
また、2次空気ブロワ24からの2次空気は、冷
却通路4を通るあいだに予熱されて、その一部が
ヘツダ25から上部バーナ16に、他部が前記熱
風発生炉6にそれぞれ至つて燃焼される。なお、
燃料として固形のコークスを使用するときは、こ
れを原石の中に一定量混入させて炉頂より投入さ
せればよく、また、微粉炭のときには空気輸送な
どでバーナに圧送させるようにすればよい。
Therefore, when firing this raw stone, the primary working air from the primary working air blower 21 is preheated by the requilifier 20, and then the primary air is supplied from the header 22 to the upper burner 16 to generate combustion air. Therefore, the working air flows through the same header 2.
2 to the injector 23 to suck in the tertiary air from the duct 26 and the combustion gas flowing back from the lower combustion chamber 7, and then reach the hot air generator 6 through the header 27 where it is combusted. Ru.
Further, the secondary air from the secondary air blower 24 is preheated while passing through the cooling passage 4, and a part of it reaches the header 25 and the upper burner 16, and the other part reaches the hot air generating furnace 6 and is combusted. be done. In addition,
When using solid coke as a fuel, it is sufficient to mix a certain amount of coke into raw stone and feed it from the top of the furnace, and when using pulverized coal, it can be forced into the burner by pneumatic conveyance. .

〔発明の効果〕 以上詳述したように、この発明によれば、円筒
状内筒に形成した円錐台状部と、この内筒周囲に
被嵌状態で設けられる円筒状外筒の円錐台対応部
に形成した膨出部との組み合わせによつて、複数
の焼成帯を構成した炉体構造としてあるので、上
下方向断面が対称形状、水平方向断面が円形状と
なつて、自立安定性に優れて転倒の恐れがすくな
くなり、部分的な補強を含めて炉体支持のための
架構の構成が簡単になり、使用鋼材の量を十分に
節減できると共に、断面積当りの所要煉瓦数もす
くなくなつて製作費の低減を図ることができ、そ
の大型化も可能であるほか、平面的な壁面とか障
害部などが形成されないために、原石およびガス
の流れに速度差、偏流などを生ずることもなく、
また円錐台状部と膨出部との組み合わせ、および
原石の流動安息角を利用して形成される空間部に
燃焼室を配するようにし、かつ、内筒内部を燃焼
用空気の予熱に利用するようにしたので、燃焼効
率を格段に向上し得るなどの有益な諸効果を有す
るものである。
[Effects of the Invention] As detailed above, according to the present invention, the truncated conical part formed in the cylindrical inner cylinder and the truncated conical part of the cylindrical outer cylinder fitted around the inner cylinder are compatible with each other. The furnace body has a structure in which a plurality of firing zones are formed by combining the bulges formed in the parts, so the cross section in the vertical direction is symmetrical and the cross section in the horizontal direction is circular, resulting in excellent self-supporting stability. The risk of overturning is reduced, the construction of the frame for supporting the furnace body, including partial reinforcement, is simplified, the amount of steel used can be sufficiently reduced, and the number of bricks required per cross-sectional area is also reduced. In addition to reducing production costs and making it possible to increase the size of the product, since there are no flat walls or obstructions, there is no difference in speed or drift in the flow of raw ore and gas. ,
In addition, the combustion chamber is arranged in the space formed by the combination of the truncated conical part and the bulging part and the flow angle of repose of the rough stone, and the inside of the inner cylinder is used for preheating the combustion air. This has various beneficial effects, such as significantly improving combustion efficiency.

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

図面はこの発明に係る焼成炉の一実施例を示す
縦断面図である。 1……円筒状内筒、2……円錐台状部、5……
熱風煙道、6……熱風発生炉、7……下部燃焼
室、8……排気煙道、11……円筒状外筒、12
……膨出部、13……上部燃焼室、16……上部
バーナ、17……循環ガス吸込口、18……取り
出し開口、19……製品取り出し装置、23……
インゼクタ、30……原石搬入コンベア、40…
…製品搬出コンベア。
The drawing is a longitudinal sectional view showing an embodiment of a firing furnace according to the present invention. 1... Cylindrical inner tube, 2... truncated conical part, 5...
Hot air flue, 6... Hot air generating furnace, 7... Lower combustion chamber, 8... Exhaust flue, 11... Cylindrical outer cylinder, 12
...Bulging part, 13... Upper combustion chamber, 16... Upper burner, 17... Circulating gas suction port, 18... Take-out opening, 19... Product take-out device, 23...
Injector, 30...Rough stone carrying conveyor, 40...
...Product delivery conveyor.

Claims (1)

【特許請求の範囲】[Claims] 1 上下方向中間部に円錐台状部を周方向に突出
した横断面円筒状の内筒と、この内筒の周囲に間
隔を置いて設けられ、前記円錐台上部に対応する
膨出部を周方向に膨出した横断面円筒状の外筒と
により炉体を構成させ、前記膨出部内の上部にバ
ーナを有する上部燃焼室、前記円錐台状部の下側
に下部燃焼室をそれぞれに形成すると共に、熱風
発生炉の煙道を前記内筒内部から前記下部燃焼室
内に開口させ、炉頂部から排気を取り出し得るよ
うにしたことを特徴とする焼成炉。
1. An inner cylinder having a cylindrical cross section with a truncated conical part protruding in the circumferential direction at the vertically intermediate portion, and a bulging part provided at intervals around the inner cylinder and surrounding the bulge corresponding to the upper part of the truncated cone. A furnace body is constituted by an outer cylinder having a cylindrical cross section that bulges in the direction, and an upper combustion chamber having a burner is formed at the upper part of the bulge, and a lower combustion chamber is formed below the truncated conical part. In addition, a firing furnace characterized in that a flue of the hot air generating furnace is opened from inside the inner cylinder into the lower combustion chamber so that exhaust gas can be taken out from the top of the furnace.
JP17213483A 1983-09-20 1983-09-20 Calciner Granted JPS6064179A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17213483A JPS6064179A (en) 1983-09-20 1983-09-20 Calciner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17213483A JPS6064179A (en) 1983-09-20 1983-09-20 Calciner

Publications (2)

Publication Number Publication Date
JPS6064179A JPS6064179A (en) 1985-04-12
JPH0143231B2 true JPH0143231B2 (en) 1989-09-19

Family

ID=15936192

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17213483A Granted JPS6064179A (en) 1983-09-20 1983-09-20 Calciner

Country Status (1)

Country Link
JP (1) JPS6064179A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006039204B4 (en) * 2006-08-22 2011-12-08 Rheinkalk Gmbh Annular shaft kiln
JP5184026B2 (en) * 2007-08-20 2013-04-17 株式会社チサキ Vertical firing furnace
US20090104635A1 (en) * 2007-10-19 2009-04-23 Tom Cheng Xu Fluorescent Dry Test Strip Biosensor

Also Published As

Publication number Publication date
JPS6064179A (en) 1985-04-12

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