JPS5923589B2 - coke oven - Google Patents

coke oven

Info

Publication number
JPS5923589B2
JPS5923589B2 JP940179A JP940179A JPS5923589B2 JP S5923589 B2 JPS5923589 B2 JP S5923589B2 JP 940179 A JP940179 A JP 940179A JP 940179 A JP940179 A JP 940179A JP S5923589 B2 JPS5923589 B2 JP S5923589B2
Authority
JP
Japan
Prior art keywords
coal
chamber
pipe
coke oven
vertical pipe
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
JP940179A
Other languages
Japanese (ja)
Other versions
JPS55102679A (en
Inventor
昌 蛭川
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP940179A priority Critical patent/JPS5923589B2/en
Publication of JPS55102679A publication Critical patent/JPS55102679A/en
Publication of JPS5923589B2 publication Critical patent/JPS5923589B2/en
Expired legal-status Critical Current

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  • Coke Industry (AREA)

Description

【発明の詳細な説明】 本発明は新しい装炭方式に基づくコークス炉に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coke oven based on a new coal charging method.

室式コークス炉の操業にあたつては、コークス炉上を運
行する装炭車をそなえ、一回の装炭量に必要な石炭量を
採炭した装炭車が所定炭室上に位置し、炉上の複数装炭
口を開いて石炭を炭室内に落下すると共に、押出機のレ
ベラーを前後して石炭を水平にならすのが常である。
When operating a room type coke oven, a coal loading car is provided that runs above the coke oven, and the coal loading car that has mined the amount of coal required for one coal loading is located above a designated coal chamber, It is customary to open multiple coal charging ports to allow coal to fall into the coal chamber, and to level the coal by moving the leveler of the extruder back and forth.

そのとき装炭口やレベラー口から飛散する黒煙、粉塵は
作業環境を汚染するので、種々な集塵装置が用いられて
いるが、作業が煩雑な上に省エネルギーの見地からも好
ましくない。そこで原料炭を配管中に気送して、均炭作
業なしに各炭室に充填する方法も案出されているが、石
炭乾燥予熱設備の設置等が必須となり、全体の設備費と
しても高額となるという難点がある。本発明はこのよう
な難点の解決をはかるべき新しい装炭設備を設けたコー
クス炉にかかるものである。つぎに本発明の実施例につ
いて説明する。
At this time, black smoke and dust scattered from the coal charging port and leveler port contaminate the working environment, so various dust collectors are used, but these devices are not only complicated to work with but also undesirable from the standpoint of energy conservation. Therefore, a method has been devised in which coking coal is pneumatically conveyed through piping and filled into each coal chamber without the need for equalizing the coal, but this requires the installation of coal drying and preheating equipment, and the overall equipment cost is high. There is a problem that. The present invention relates to a coke oven equipped with a new coal charging equipment that is intended to solve these difficulties. Next, embodiments of the present invention will be described.

コークス炉の炉上各炭室のほぼ中央部に各炭室ごとに石
炭が貯蔵される密閉容器4を設ける。密閉容器4の上部
には密閉輸送径路が設けられる。たとえばダクト1内に
チエンコンベャ2を設け、ダクトフ 1には開閉自在の
シュート3を設ける。ダクト1及び密閉容器4内には常
に不活性ガスが注入され、シュート3は輸送した石炭を
落下すべき炭室に相当する密閉容器上で開、その他の密
閉容器上では閉じられている。密閉容器下部には装入シ
ュート55が連結し、装入シュート5に接続して斜下方
に延出する二又の傾斜管8、8が分岐する。傾斜管8、
8が分岐した装入シュートの下部は垂直管6は炭室13
の頂部煉瓦を貫通する垂直路15内に垂直路15との間
に間隔がないように、また傾斜0管8、8はその延長線
が炭室上部煉瓦を貫通する傾斜路16、16内に延長し
て傾斜路16との間に間隔がないように保持されている
。なお二又の傾斜管は必要に応じて更に二又を加えた傾
斜管とし、これらの延長線に同様な炭室上部煉瓦を貫通
5 する傾斜路を設けて接続してもよい。更に垂直管6
及び傾斜管8、8の間を連結する連結管10を設ける。
T及び9はそれぞれ装入シュート5及び傾斜管8に設け
たダンパーである。11は傾斜管の掃除口であり、12
は不活性ガスの導入口であ07.0なお図中13は炭室
、14は炭室頂部煉瓦、ITは上昇管である。
A closed container 4 in which coal is stored in each coal chamber is provided approximately at the center of each coal chamber above the coke oven. A closed transport path is provided in the upper part of the closed container 4. For example, a chain conveyor 2 is provided in a duct 1, and a chute 3 that can be opened and closed is provided in the duct 1. Inert gas is always injected into the duct 1 and the closed container 4, and the chute 3 is opened over the closed container corresponding to the coal chamber into which the transported coal is to be dropped, and closed over the other closed containers. A charging chute 55 is connected to the lower part of the closed container, and bifurcated inclined pipes 8, 8 are connected to the charging chute 5 and extend diagonally downward. Inclined pipe 8,
At the bottom of the charging chute where 8 is branched, the vertical pipe 6 is connected to the coal chamber 13.
The vertical passages 15 passing through the top brick of the coal chamber have no spacing between them, and the inclined zero pipes 8, 8 have their extension lines within the ramps 16, 16 passing through the top brick of the coal chamber. It extends and is maintained so that there is no gap between it and the ramp 16. In addition, the two-pronged inclined pipe may be made into an inclined pipe with further two prongs added thereto as necessary, and an extended line thereof may be connected by providing a ramp passing through the same brick above the coal chamber. Further vertical pipe 6
A connecting pipe 10 is provided to connect the inclined pipes 8, 8.
T and 9 are dampers provided on the charging chute 5 and the inclined pipe 8, respectively. 11 is a cleaning port of the inclined pipe; 12
07.0 is the inert gas inlet. In the figure, 13 is the coal chamber, 14 is the brick at the top of the coal chamber, and IT is the riser pipe.

次に本発明にかかるコークス炉の装炭方法について述べ
る。
Next, a method for charging a coke oven according to the present invention will be described.

従来のコークス炉操業においては1つの炭室の乾留が完
了すればコークスの排出が行5 なわれる。ついで装炭
車による石炭の装炭が行なわれ、装炭の完了と同時に新
しく装炭された石炭の乾留が開始する。ついで次に排出
すべき炭室か7【−らのコークスの排出が行なわれるの
であるが、このような作業の一行程として、装炭はきわ
めて短時間のうちに完了する必要があり、装炭車によつ
て行なうことが必須作業となつている。
In conventional coke oven operation, coke is discharged once carbonization in one coal chamber is completed. Next, coal is loaded using a coal loading car, and at the same time as coal loading is completed, carbonization of the newly loaded coal begins. Next, the coke from the coal chamber 7 [-] to be discharged is discharged, but as one step of this work, coal loading must be completed in an extremely short time, and the coal loading car It has become essential work to be carried out by

本発明においては従来の装炭車を用いることなく、しか
も従来の装炭車のようにつぎの炭室に装炭するためどう
しても移動しなければならない機器を用いないため、装
炭作業の基本的考えを全く新しくする。すなわち一つの
炭室について相当時間をかけて装炭しても決して他の炭
室の装炭作業について障害を与えることはない。それぞ
れ炭室毎に固定的に設けられた密閉容器があるので、密
閉容器と炭室とを一体的に利用して長時間をかけて装炭
しても何らの不都合を生じない。本発明による装炭方法
の一例を述べれば、コークスの排出が完了した炭室には
ダクト1内のチエンコンベヤ2上を輸送される石炭が密
閉容器4、装入シュート5及び垂直管6を通じて急速に
炭室13内に装入される。
In the present invention, a conventional coal loading car is not used, and unlike conventional coal loading cars, equipment that must be moved in order to load coal into the next coal chamber is not used, so the basic idea of coal loading work is improved. Make it completely new. In other words, even if it takes a considerable amount of time to load one coal chamber, it will never interfere with the loading work of other coal chambers. Since there is a sealed container fixedly provided for each charcoal chamber, no inconvenience will occur even if the sealed container and the charcoal chamber are used integrally to carry out carbonization over a long period of time. To describe an example of the coal loading method according to the present invention, coal transported on a chain conveyor 2 in a duct 1 is rapidly transported to a coal chamber after coke discharge through a closed container 4, a charging chute 5 and a vertical pipe 6. The charcoal is charged into the charcoal chamber 13.

そのとき石炭は一定の安息角で堆積するのでL1のレベ
ルまで装入される。その後はたとえばダンパー7を閉じ
、ダンパー9を開くと石炭は傾斜管を流れ、炭室内でL
2のレベルまで装入される。排炭後の装炭作業は一応こ
の段階で終止し、その後はチエンコンベヤ2で送られて
きた石炭は一応密閉容器4中に貯蔵されて、当初炭室内
に装入しなければならない予定炭量とL2のレベルまで
の炭量の差が密閉容器4内に貯蔵されていることとなる
。なお密閉容器はシュート3を閉じることによつて外部
と絶縁され、また必要に応じて不活性ガスを充満してお
くのが望ましい。乾留が進行して炭室内の温度が上昇す
れば既に炭室内に装入された石炭中の水分が蒸発し、炭
室壁よりの伝熱によつて一部石炭の溶融やガス発生によ
る堆積石炭の変形が生じて炭室内の石炭レベルにも変動
が生ずる。このとき石炭は傾斜管8等を満たして炭室上
の密閉容器にまで充填されているので、炭室内に生じた
空隙を充填する分だけ石炭が炭室内に落下する。更に乾
留が開始されて発生したガスやL1とL2の山の谷間に
残つていた空隙中のガスは加熱されてL2の頂部と炭室
上部煉瓦14の間を流出し、一部は連結管10を通じて
傾斜管8中に流出し、また12を微量の不活性ガス源と
連結しておけば、不活性ガスの流出もあつて石炭レベル
L2がL3にまで自然にならされる。この時点でダンパ
ー9の開度を小さくすれば傾斜管8から装入される石炭
はガス流に乗つて移動し、L3のレベルに達する。これ
により当初子定していた必要量の石炭の装入が終了する
こととなる。以上説明したように本発明にかかるコーク
ス炉によるときは、(1)石炭の装入に際し均炭作業を
必要としないため、完全密閉状態で作業が可能である。
At that time, coal is deposited at a constant angle of repose, so it is charged up to the level of L1. After that, for example, when the damper 7 is closed and the damper 9 is opened, the coal flows through the inclined pipe and the L in the coal chamber.
Charged up to level 2. The coal loading work after coal discharge ends at this stage, and after that, the coal sent by chain conveyor 2 is temporarily stored in airtight container 4, and the planned amount of coal that must be initially charged into the coal chamber is This means that the difference in the amount of coal up to the level of L2 is stored in the closed container 4. The closed container is preferably insulated from the outside by closing the chute 3, and filled with inert gas as necessary. As carbonization progresses and the temperature inside the coal chamber rises, the moisture in the coal that has already been charged into the coal chamber evaporates, and some of the coal melts due to heat transfer from the coal chamber wall, and the coal piles up due to gas generation. deformation occurs, and the coal level in the coal chamber also fluctuates. At this time, since the coal fills the inclined pipe 8 and the like to the closed container above the coal chamber, the amount of coal that fills the voids created in the coal chamber falls into the coal chamber. Furthermore, the gas generated when carbonization starts and the gas remaining in the gap between the peaks of L1 and L2 are heated and flow out between the top of L2 and the coal chamber upper brick 14, and some of it flows into the connecting pipe. If the coal flows out through 10 into the inclined pipe 8, and 12 is connected to a trace amount of inert gas source, the inert gas flows out and the coal level L2 is naturally leveled to L3. If the opening degree of the damper 9 is reduced at this point, the coal charged from the inclined pipe 8 will move along with the gas flow and reach the level L3. This will complete the charging of the required amount of coal that was initially determined. As explained above, when using the coke oven according to the present invention, (1) there is no need for equalizing work when charging coal, so work can be performed in a completely sealed state.

そのため大気汚染防止設備を必要としない。(2)装炭
末期の石炭は、炭室ごとに個別に設けた密閉容器により
長時間かけて装入することができ、そのとき乾留ガスに
より乾燥、予熱されることによつて装入はスムーズに進
行し、乾留時間も短縮されるので乾留の遂行上不都合を
生ずることはない。
Therefore, air pollution prevention equipment is not required. (2) Coal at the final stage of coalization can be charged over a long period of time in sealed containers installed individually in each coal chamber, and the charging is smooth because it is dried and preheated by carbonization gas. Since the carbonization time is shortened, there is no problem in carrying out the carbonization.

(3)原料炭が湿炭であつても装入できるので、石炭の
乾燥、予熱設備が不要で、しかも一部炉温の上昇を利用
して乾燥効果を発揮せしめることもできる。
(3) Even if the coking coal is wet coal, it can be charged, so there is no need for coal drying or preheating equipment, and the drying effect can also be achieved by partially utilizing the rise in furnace temperature.

また石炭の乾燥予熱設備を併用した場合は乾留温度の変
更もなく稼動率を変更することも可能であり、炉温変更
による悪影響なしに生産量の調整ができる等のFfl3
,点を有している。
In addition, when coal drying and preheating equipment is used in conjunction, it is also possible to change the operating rate without changing the carbonization temperature, making it possible to adjust the production amount without adverse effects due to changing the furnace temperature.
, has points.

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

図面は本発明の実施態様の一例で第1図はその概念を示
す断面図の一部、第2図は同じく部分拡大断面図である
。 2・・・・・・チエンコンベャ、4・・・・・・密閉容
器、5・・・・・・装入シュート、6・・・・・・垂直
管、7,9・・・・・・ダンパー、8・・・・・・傾斜
管、13・・・・・・炭室、14・・・・・・炭室頂部
煉瓦。
The drawings are an example of an embodiment of the present invention, and FIG. 1 is a partial sectional view showing the concept thereof, and FIG. 2 is a partially enlarged sectional view. 2...Chain conveyor, 4...Tight container, 5...Charging chute, 6...Vertical pipe, 7,9...Damper , 8... Inclined pipe, 13... Coal chamber, 14... Coal chamber top brick.

Claims (1)

【特許請求の範囲】[Claims] 1 コークス炉炭室上に密閉輸送径路上を輸送される石
炭が貯蔵される密閉容器と、該密閉容器から炭室頂部煉
瓦を貫通する垂直路に接続する垂直管と、該垂直管より
分岐して斜下方に延出し、その延長線が炭室上部煉瓦を
貫通する傾斜路に接続する二又の傾斜管を有し、前記垂
直管ならびに傾斜管の間を連結する連結管を備え、垂直
管及び傾斜管には通過する石炭流量を調節するダンパー
と、不活性ガスの注入口を備えたコークス炉。
1. A closed container in which coal is stored on a closed transportation route above the coke oven coal chamber, a vertical pipe connected from the closed container to a vertical passage passing through the top brick of the coal chamber, and a vertical pipe branching from the vertical pipe. The vertical pipe has a two-pronged inclined pipe which extends diagonally downward and whose extension line connects to a ramp passing through the upper brick of the coal chamber, and a connecting pipe which connects the vertical pipe and the inclined pipe. and a coke oven equipped with a damper to adjust the flow rate of coal passing through the inclined pipe and an inert gas inlet.
JP940179A 1979-01-29 1979-01-29 coke oven Expired JPS5923589B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP940179A JPS5923589B2 (en) 1979-01-29 1979-01-29 coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP940179A JPS5923589B2 (en) 1979-01-29 1979-01-29 coke oven

Publications (2)

Publication Number Publication Date
JPS55102679A JPS55102679A (en) 1980-08-06
JPS5923589B2 true JPS5923589B2 (en) 1984-06-02

Family

ID=11719389

Family Applications (1)

Application Number Title Priority Date Filing Date
JP940179A Expired JPS5923589B2 (en) 1979-01-29 1979-01-29 coke oven

Country Status (1)

Country Link
JP (1) JPS5923589B2 (en)

Also Published As

Publication number Publication date
JPS55102679A (en) 1980-08-06

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