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JPH07100793B2 - Extraction method and equipment for coke oven charging - Google Patents
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JPH07100793B2 - Extraction method and equipment for coke oven charging - Google Patents

Extraction method and equipment for coke oven charging

Info

Publication number
JPH07100793B2
JPH07100793B2 JP28509690A JP28509690A JPH07100793B2 JP H07100793 B2 JPH07100793 B2 JP H07100793B2 JP 28509690 A JP28509690 A JP 28509690A JP 28509690 A JP28509690 A JP 28509690A JP H07100793 B2 JPH07100793 B2 JP H07100793B2
Authority
JP
Japan
Prior art keywords
coal
charging
carbonization chamber
carbonization
furnace
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 - Fee Related
Application number
JP28509690A
Other languages
Japanese (ja)
Other versions
JPH04159391A (en
Inventor
恵三 井上
邦彦 西岡
潔 三浦
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP28509690A priority Critical patent/JPH07100793B2/en
Publication of JPH04159391A publication Critical patent/JPH04159391A/en
Publication of JPH07100793B2 publication Critical patent/JPH07100793B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 この発明は、室炉式コークス炉の炭化室に装入された水
分を含む装入炭の炭層中に、炭化室上部空間に通じる水
蒸気の抽気孔を開孔する方法ならびにその装置に関す
る。
Description: TECHNICAL FIELD The present invention relates to a steam extraction hole for steam leading to the upper space of a carbonization chamber in a coal seam of a charging coal containing moisture charged in a carbonization chamber of a chamber coke oven. And a device therefor.

従来の技術 室炉式コークス炉によるコークスの製造法においては、
炭化室に装入された装入炭は、両側の燃焼室から炉壁を
介して間接加熱され、コークス化される。この炭化室は
コークスの排出を考慮してテーパを持たせ、マシンサイ
ドよりコークサイドの炉幅を50〜70mm程度広く設定して
いる。このため、20〜30余のフリュー列からなる燃焼室
は、炭化室とは逆にコークサイドがマシンサイドより幅
が50〜70mm広い。また、燃焼室の温度は、マシンサイド
よりコークサイドの方を炉幅のテーパに合せ50〜100℃
程度高く設定し、炉長方向でのコークス化の均一化を図
っている。
Conventional technology In the method of producing coke with a chamber-type coke oven,
The charging coal charged in the carbonization chamber is indirectly heated from the combustion chambers on both sides via the furnace wall and is converted into coke. This carbonization chamber has a taper in consideration of the discharge of coke, and the furnace width on the coke side is set to be 50 to 70 mm wider than the machine side. For this reason, in the combustion chamber consisting of 20 to 30 or more flue rows, the coke side is 50 to 70 mm wider than the machine side, as opposed to the carbonization chamber. Also, the temperature of the combustion chamber is 50 to 100 ° C depending on the taper of the furnace width on the coke side rather than the machine side.
The coke formation in the furnace length direction is made uniform by setting it to a high level.

しかしながら、コークス炉炭化室への装入炭の装炭作業
は、一般に装炭車のホッパーから炉上の装炭口を介して
自然落下により行なわれている。このため、落下時の衝
撃を受ける装炭口直下は、落下時の衝撃を受けない装炭
口と装炭口との間、あるいは炉蓋側に比較して装入嵩密
度が高く、炉長方向でのコークス化の均一化を阻害して
いる。
However, the coal-charging work of charging the coke-furnace carbonization chamber is generally performed by a natural drop from a hopper of a coal-charging vehicle through a coal-charging port on the furnace. For this reason, the area directly below the coal charging port that receives the impact when dropped has a higher charging bulk density than the space between the coal charging port that does not receive the impact when falling and the furnace lid side. This hinders the uniformization of coking in the direction.

近年、コークス炉の乾留効率化と炉体延命化とを図りな
がら、コークス品質の安定向上を達成することが要求さ
れており、そのための技術開発が進められている。
In recent years, it has been required to achieve stable improvement of coke quality while improving the efficiency of dry distillation of the coke oven and prolonging the life of the furnace body, and technical development for that purpose is being advanced.

コークス炉の乾留効率の向上と炉体の延命化とは相反す
る要求であり、これらを両立させることは容易なことで
はない。例えば、乾留効率の向上を図る方法としては、
通常8〜10%含有されている装入炭の全水分を5〜6%
に低減する調湿炭装入法、および装入炭を170〜250℃ま
で乾燥予熱して全水分を2%以下に低減する予熱炭装入
法が知られている。
Improving the carbonization efficiency of a coke oven and prolonging the life of the furnace are contradictory requirements, and it is not easy to make them compatible. For example, as a method to improve the distillation efficiency,
The total water content of the charged coal, which is usually 8-10%, is 5-6%.
There is known a method for charging a conditioned coal which reduces the amount to 2%, and a method for charging a preheated coal which reduces the total water content to 2% or less by drying and preheating the charged coal to 170 to 250 ° C.

これらの技術は、乾留所要時間短縮によるコークス炉生
産性の向上、装入嵩密度の増大と乾留中の石炭の軟化溶
融層幅の拡大によるコークス化性の改善向上、乾留所要
熱量の低減を図ることができる。しかし、一方では装入
炭の乾燥あるいは予熱のために莫大な設備投資を必要と
する問題がある。
These technologies aim to improve the productivity of coke ovens by shortening the time required for carbonization, increase the bulk density of the charge and improve the coke formation by expanding the width of the softening and melting layer of coal during carbonization, and reduce the amount of heat required for carbonization. be able to. However, on the other hand, there is a problem that enormous capital investment is required for drying or preheating the charged coal.

このため、調湿炭装入法や予熱炭装入法は、一般に普及
するに至らず、一部のコークス工場に採用されるに止ど
まっているのが実情である。
For this reason, the humidified coal charging method and the preheated coal charging method have not come into widespread use, and the fact is that they are used only in some coke plants.

さらに、調湿炭装入法や予熱炭装入法は、装入嵩密度が
増大するため、乾留の際に炉壁へ大きな石炭膨脹圧がか
かり、炉壁を損傷する虞がある。
Further, in the humidified coal charging method and the preheated coal charging method, since the bulk density of charging increases, a large coal expansion pressure is applied to the furnace wall during carbonization, which may damage the furnace wall.

また、乾留効率を向上する方法としては、炉幅あるいは
炉高を拡大する検討もなされているが、これらは新規に
コークス炉を設置する場合に有効ではあるが、既設のコ
ークス炉に適用できないため、既設炉の乾留効率化には
つながらない。
Also, as a method of improving the carbonization efficiency, it has been studied to expand the furnace width or furnace height, but these are effective when a new coke oven is installed, but cannot be applied to an existing coke oven. , It does not lead to the improvement of the efficiency of dry distillation of the existing furnace.

さらに、炉壁煉瓦を薄くして伝熱性を改善する方法も、
一部実用化されているが、これは炉体の堅牢性を損う虞
があって、必ずしも採用できるとは限らない。
Furthermore, the method of improving the heat conductivity by making the furnace wall brick thinner,
Although it has been partially put into practical use, this may impair the robustness of the furnace body and cannot always be adopted.

一方、炉体の延命化を実現する最も簡便な方法は、炉温
を下げて低負荷操業を実施することであるが、これは乾
留効率の向上を逆行することは言うまでもない。また、
近年の補修技術の進歩は、炉体寿命の増大に大きな効果
を上げているが、これは損傷した炉体の補修であって、
事後処理の技術である。
On the other hand, the simplest method for extending the life of the furnace body is to lower the furnace temperature and carry out a low-load operation, but it goes without saying that this reverses the improvement of the carbonization efficiency. Also,
Recent advances in repair technology have had a great effect on increasing the life of the furnace body, which is the repair of damaged furnace bodies.
It is a post-processing technology.

したがって、乾留効率の向上と炉体の延命化とを両立さ
せながら、コークス品質の安定向上を達成することは、
極めて難しい問題である。
Therefore, it is possible to achieve stable improvement of coke quality while achieving both improvement of carbonization efficiency and prolongation of life of the furnace body.
This is a very difficult problem.

本発明者らは、装入炭に8〜11%含有される水分の乾留
過程における脱水挙動に着目し研究を行った。その結
果、水分を含有する装入炭を乾留する際の乾留効率が低
下する原因は、乾留初期に石炭層内で発生する水蒸気の
壁側への流れにあることを見い出した。そこでその流れ
を高温の炉壁(少なくとも1000℃以上)方向から低温の
炭化室上部空間部(750〜850℃)方向に変えれば、炉壁
から炭層中への伝熱効率の改善と、炉壁への膨脹圧を抑
制できることを確認した。そして炭化室に装入された水
分を含有する装入炭の上面を、レベリングしたのち炉上
の装炭口から開孔部材を炉内の石炭層内に差込み、これ
を引抜くことにより炭化室上部空間部に通じる抽気孔を
設けることができ、乾留初期に発生する水蒸気の流れを
炭化室上部空間方向に変換できることを究明し、既に特
願昭63−299173号として特許出願している。
The present inventors have conducted a study focusing on the dehydration behavior of the water contained in the charged coal in an amount of 8 to 11% during the carbonization process. As a result, it was found that the cause of the decrease in the carbonization efficiency when carbonizing the charged coal containing water is the flow of water vapor generated in the coal bed at the initial stage of carbonization to the wall side. Therefore, if the flow is changed from the high temperature furnace wall (at least 1000 ° C or higher) to the low temperature carbonization chamber upper space (750 to 850 ° C), the heat transfer efficiency from the furnace wall to the coal bed is improved and It was confirmed that the expansion pressure of 1 could be suppressed. Then, after leveling the upper surface of the charged coal containing water charged in the carbonization chamber, the opening member is inserted into the coal layer in the furnace from the coal charging port on the furnace, and the carbonization chamber is pulled out. It was clarified that a bleeding hole communicating with the upper space can be provided, and the flow of steam generated in the initial stage of carbonization can be converted to the upper space direction of the carbonization chamber, and a patent application has already been filed as Japanese Patent Application No. 63-299173.

発明が解決しようとする課題 前記炭化室に装入された装入炭の上面をレベリングした
のち、石炭層中に炭化室上部空間に通じる抽気孔を開孔
するには、炉上の装炭口から開孔部材を炉内の石炭内に
差込み、引抜くのが最も簡便で、装炭車に開孔部材およ
び該開孔部材の上下機構からなる抽気孔開孔装置を付設
することにより解決できる。しかしながら、装炭車に抽
気孔開孔装置を付設しても、抽気孔の形成は装炭口の個
数により制限されるという難点がある。
Problems to be Solved by the Invention After leveling the upper surface of the charging coal charged in the carbonization chamber, in order to open an extraction hole leading to the upper space of the carbonization chamber in the coal bed, a charging port on the furnace is used. The simplest method is to insert the hole opening member into the coal in the furnace and pull out, and this can be solved by attaching a bleed hole hole opening device including a hole opening member and a vertical mechanism of the hole opening member to the coal charging car. However, even if a bleeding hole opening device is attached to the coal car, the formation of the bleed hole is limited by the number of coal blasting ports.

すなわち、4〜5個の装炭口に対応して形成される4〜
5個の抽気孔では、装入炭から発生する水蒸気量に対
し、十分な抽気能力を得ることは困難で、乾留効率の向
上および炉体の延命化を阻害する炉壁に向かう水蒸気の
流れを、常時十分に抑制することができない。また、常
に装炭口下の同一位置にしか開孔できず、窯口部等の炉
内低温部近傍に抽気孔を開孔できない。さらにコークス
炉のヒートパターンは、均一ではなく、窯口部以外にも
炉団によっては低温部が出現する場合がある。
That is, 4 to 5 formed corresponding to 4 to 5 coal charging ports
With the five extraction holes, it is difficult to obtain sufficient extraction capacity for the amount of steam generated from the charging coal, and the steam flow toward the furnace wall that hinders improvement of carbonization efficiency and extension of life of the furnace body , Cannot always be sufficiently suppressed. Moreover, the holes can always be opened only at the same position under the coal charging port, and the extraction holes cannot be opened near the low temperature part in the furnace such as the kiln port. Furthermore, the heat pattern of the coke oven is not uniform, and a low temperature part may appear depending on the furnace group other than the kiln mouth part.

この発明は、かかる現状に鑑み、装入炭層中に任意に傾
斜した抽気孔を設けることにより、乾留初期に装入炭の
含有水分に基づき発生する水蒸気などを十分に抽気でき
る抽気孔の開孔方法およびその装置を提供するものであ
る。
In view of the present situation, the present invention provides a bleed hole which can sufficiently bleed off steam and the like generated based on the water content of the charged coal in the initial stage of carbonization by providing an arbitrarily inclined bleed hole in the charged coal layer. A method and apparatus therefor are provided.

課題を解決するための手段 本発明者らは、前記目的を達成するため鋭意検討を行っ
た。その結果、コークス炉の窯出し作業は、通常5窯ピ
ッチあるいは数窯ピッチで行なわれており、装炭作業位
置で前回装炭された炭化室位置に、装入蓋蓋取装置、開
孔部材および該開孔部材の上下駆動機構からなる抽気孔
開孔装置、抽気孔開孔装置の傾動機構を付設し、開孔部
材を装炭口中心を通る鉛直線を含む炉長方向断面内で、
鉛直線に対し5゜以上40゜以下の角度で炭化室内の装入
炭層中に差込み、直ちに引抜いて抽気孔を形成しても、
崩れることなく抽気孔が保持されることを確認した。
Means for Solving the Problems The inventors of the present invention have made extensive studies to achieve the above object. As a result, the coke oven kiln removal work is usually performed at a 5 kiln pitch or several kiln pitches, and the charging lid lid removing device and the opening member are placed at the carbonization chamber position where the coal was previously carbonized at the carbonization work position. And a bleeding hole opening device consisting of a vertical drive mechanism of the opening member, the tilting mechanism of the bleeding hole opening device is attached, and the opening member in the furnace length direction cross section including a vertical line passing through the center of the coal charging port,
Even if it is inserted into the charging coal layer in the carbonization chamber at an angle of 5 ° or more and 40 ° or less with respect to the vertical line and immediately extracted to form a bleed hole,
It was confirmed that the bleed holes could be retained without collapsing.

また、抽気孔開孔装置の上端は、装炭車の受炭走行時の
石炭塔下面で制約されるので、給炭ホッパー上端より下
部に位置する必要がある。しかし、前回装入窯位置に設
置するから装炭車の炉団方向端部に抽気孔開孔装置が設
置され、上下駆動機構を炉上近傍に設置できるため、1
本の開孔部材で十分な深さの抽気孔を開孔することがで
きる。
Further, since the upper end of the bleed hole opening device is restricted by the lower surface of the coal tower during the coal receiving operation of the coal car, it is necessary to be located below the upper end of the coal feeding hopper. However, since it was installed in the charging kiln position last time, a bleeder hole opening device is installed at the end of the coal charging car in the furnace group direction, and the vertical drive mechanism can be installed near the furnace.
It is possible to open a bleed hole having a sufficient depth with a book opening member.

さらに、抽気孔開孔装置は、装炭作業のために停止した
装炭車上の前回装入窯位置に設置したから、抽気孔開孔
作業を装炭作業中に行うことができる。
Further, since the extraction hole opening device is installed at the previous charging kiln position on the coal charging vehicle stopped for the carbonization operation, the extraction hole opening operation can be performed during the carbonization operation.

また、抽気孔開孔作業時に装炭口から噴出する発塵、火
炎の問題については、装炭時の発塵防止のため実施され
ている上昇管への高圧安水の噴射を継続し、炭化室内を
負圧に維持することにより解決できることを究明し、こ
の発明に到達した。
Regarding the problem of dust and flame ejected from the coal charging port during the bleeding hole opening work, the high-pressure ammonium water is continuously injected into the rising pipe to prevent dust generation during carbonization, and carbonization is continued. The inventors have found that the problem can be solved by maintaining a negative pressure in the room, and arrived at the present invention.

すなわちこの発明は、室炉式コークス炉の炭化室に装入
された水分を含む装入炭の表面から、装入炭層中に炭化
室上部空間と通じる抽気孔を開孔する方法において、装
炭口中心を通る鉛直線を含む炉長方向断面内で、鉛直線
に対し5゜以上40゜以下の角度で炭化室内の装入炭層中
に1ないし複数本の抽気孔を設けるのである。
That is, the present invention relates to a method of opening a bleed hole communicating with the upper space of the carbonization chamber in the charging coal layer from the surface of the charging coal containing water charged in the carbonization chamber of the chamber furnace type coke oven. Within the cross section of the furnace length direction including the vertical line passing through the center of the mouth, one or a plurality of bleed holes are provided in the coal bed in the carbonization chamber at an angle of 5 ° or more and 40 ° or less with respect to the vertical line.

また、室炉式コークス炉の炭化室に装入された水分を含
む装入炭の表面から、装入炭層中に炭化室上部空間と通
じる抽気孔を開孔する装置において、装炭位置に停止し
た装炭車の前回の装炭窯位置に装入蓋蓋取装置、開孔部
材とその上下動駆動手段からなる抽気孔開孔装置および
該抽気孔開孔装置の傾動機構を設置したのである。
In addition, in a device that opens a bleed hole that communicates with the upper space of the carbonization chamber in the coal bed from the surface of the coal containing water charged in the carbonization chamber of the chamber furnace coke oven, stop at the carbonization position. The charging lid lid removing device, the bleeding hole piercing device including the piercing member and the vertical movement driving means, and the tilting mechanism of the bleeding hole piercing device are installed at the previous position of the coal unloading car of the coal unloading car.

作用 この発明においては、装炭口中心を通る鉛直線を含む炉
長方向断面内で、鉛直線に対し5゜以上40゜以下の角度
で炭化室内の装入炭層中に1ないし複数本の抽気孔を設
けるので、各装炭口あたりの抽気孔開孔数を従来の2〜
3倍に増加させることができ、石炭層内部に発生する水
蒸気量に対し、十分な抽気能力を得ることができ、乾留
効率の向上効果を発揮することができる。
Effect In the present invention, one or a plurality of extractions are made in the charging layer in the carbonization chamber at an angle of 5 ° or more and 40 ° or less with respect to the vertical line in the cross section of the furnace length direction including the vertical line passing through the center of the charging port. Since the pores are provided, the number of bleed holes per charging port can be set to 2
It can be increased three times, a sufficient extraction capacity can be obtained for the amount of water vapor generated inside the coal bed, and the effect of improving the carbonization efficiency can be exhibited.

なお、抽気孔の開孔角度を装炭口中心を通る鉛直線を含
む炉長方向断面内で、鉛直線に対し5゜以上、40゜以下
としたのは、5゜以下の角度では左右2本の抽気孔を開
孔する際に、2本目の抽気孔が1本目に近接するため、
両方の抽気孔が崩れて正常に抽気孔を設けることができ
ない。また、40゜以上の角度では装炭口から開孔部材を
挿入できなくなるからである。
In addition, the opening angle of the bleed hole was set to 5 ° or more and 40 ° or less with respect to the vertical line in the furnace length direction cross section including the vertical line passing through the center of the coal charging port. When opening the bleed hole of the book, the second bleed hole is close to the first,
Both bleed holes collapse and the bleed holes cannot be normally provided. Also, if the angle is 40 ° or more, the aperture member cannot be inserted from the coal charging port.

また、装炭位置に停止した装炭車の前回の装炭窯位置に
装入蓋蓋取装置、開孔部材とその上下動駆動手段からな
る抽気孔開孔装置および該抽気孔開孔装置の傾動機構を
設置したので、装炭作業中に前回装炭した炭化室の装入
蓋を蓋取装置により取外し、抽気孔開孔装置を傾動機構
により所定角度に傾動させ、開孔部材を上下駆動手段を
介して装入炭中に挿入、上昇せしめることを繰返せば、
各装炭口毎に数本の抽気孔を開孔することができる。
Further, at a previous coal-charging kiln position of the coal-charging vehicle stopped at the coal-charging position, a charging-lid lid removing device, a bleed-hole piercing device including a piercing member and a vertical movement driving means, and a tilting mechanism of the bleed-hole piercing device. Since the installation lid was installed, the charging lid of the carbonization chamber that was previously carbonized during the carbonization work was removed by the lid removing device, and the bleeding hole opening device was tilted at a predetermined angle by the tilting mechanism, and the hole opening member was moved up and down. Inserting into the charging coal through
Several bleed holes can be opened for each charging port.

傾動機構としては、抽気孔開孔装置を下部の枢軸を中心
に傾動できるものであればよく、モーターと歯車の組合
せ、あるいはアクチェータとリンク機構の組合せ等いず
れも使用することができる。
The tilting mechanism may be any one that can tilt the bleed hole opening device about the lower pivot, and may be a combination of a motor and a gear, a combination of an actuator and a link mechanism, or the like.

開孔する抽気孔の深さは、乾留時水蒸気の流れを阻害す
る石炭の軟化層が、装入された装入炭の上面から50cmを
超えない範囲に形成されることから、50cm以上あればよ
い。
The depth of the bleed hole to be opened is 50 cm or more because the softening layer of coal that inhibits the flow of steam during carbonization is formed in a range not exceeding 50 cm from the upper surface of the charged coal. Good.

また、抽気孔の大きさは、前記軟化層の膨張により、抽
気孔が閉塞されないよう30mm以上とすべきである。
Further, the size of the extraction hole should be 30 mm or more so that the extraction hole is not blocked by the expansion of the softening layer.

この発明においては、石炭装入中に水蒸気抽出のための
抽気孔が開孔され、抽気孔開孔のために余分な作業時間
を費し、コークス炉の窯出作業を遅延させることもな
い。
In the present invention, the extraction hole for steam extraction is opened during the charging of coal, extra work time is consumed for opening the extraction hole, and the coke oven kiln removal work is not delayed.

実施例 実施例1 この発明の抽気孔開孔方法ならびに開孔装置について、
実施の一例を示す第1図ないし第3図に基づいて詳細に
説明する。
Example 1 An extraction hole opening method and an opening device of the present invention,
A detailed description will be given based on FIGS. 1 to 3 showing an example of the embodiment.

コークス炉(1)の炉上に敷設されたレール(2)上に
は、装炭車(3)が走行自在に載置されている。この装
炭車(3)には、装入炭を炭化室(4)に装入するため
の複数の給炭ホッパー(5)が設けられている。
On a rail (2) laid on the furnace of the coke oven (1), a coal car (3) is movably placed. The coal car (3) is provided with a plurality of coal feed hoppers (5) for charging the charged coal into the carbonization chamber (4).

また、装炭車(3)の炉団方向の前回の装入炭化室位置
には、装入蓋(6)の蓋取装置(19)、抽気孔開孔装置
(20)および抽気孔開孔装置(20)の傾動機構(33)が
付設されている。この抽気孔開孔装置(20)は、ガイド
パイプ(21)とガイドローラー(22)、下部ガイドパイ
プ(23)に支持されたラック(24)を有する開孔部材
(25)、上下駆動用モーター(26)、上部位置センサー
(27)、下部位置センサー(28)、開孔部材(25)のス
カーフィングノズル(29)および架台(30)からなり、
下部を支点として傾動用モーター(33)により装炭口中
心を通る鉛直線を含む炉長方向断面上で角度5゜から40
゜まで自由に傾動するよう構成されている。
Further, at the position of the previous charging / charging chamber in the direction of the furnace group of the coal charging vehicle (3), the lid removing device (19) of the charging lid (6), the bleed hole opening device (20) and the bleed hole opening device The tilting mechanism (33) of (20) is attached. This bleeding hole opening device (20) includes a guide pipe (21), a guide roller (22), an opening member (25) having a rack (24) supported by a lower guide pipe (23), and a vertical drive motor. (26), upper position sensor (27), lower position sensor (28), opening member (25) scarfing nozzle (29) and frame (30),
With the tilting motor (33) with the lower part as the fulcrum, an angle of 5 ° to 40 on the furnace lengthwise cross section including the vertical line passing through the center of the coal charging port.
It is configured to tilt freely up to °.

この開孔部材(25)は、ガイドパイプ(21)、ガイドロ
ーラー(22)および下部ガイドパイプ(23)によって位
置決めされており、上部位置センサー(27)および下部
位置センサー(28)によって、所定深度の抽気孔(31)
を形成すべくその上下ストロークが決定される。また、
上下駆動用モーター(26)には、第3図に示すとおり開
孔部材(25)の側部長手方向に設けられたラック(24)
に噛み合うように歯車(32)が設けられ、開孔部材(2
5)の駆動速度は、例えば1m/秒としてある。また、ラッ
ク(24)は、抽気孔(31)を開孔したのち、上部へ移動
する間スカーフィングノズル(29)から噴射される圧縮
空気により、付着した装入炭の清掃と冷却が同時に行な
われるように構成する。
The hole member (25) is positioned by the guide pipe (21), the guide roller (22) and the lower guide pipe (23), and the predetermined position by the upper position sensor (27) and the lower position sensor (28). Bleed holes for (31)
The vertical stroke is determined to form Also,
As shown in FIG. 3, the vertical drive motor (26) has a rack (24) provided in the longitudinal direction of the side of the aperture member (25).
The gear (32) is provided so as to mesh with the opening member (2).
The driving speed of 5) is, for example, 1 m / sec. Further, the rack (24) has the extraction hole (31) opened, and then while moving to the upper portion, cleaning and cooling of the adhering charging coal are simultaneously performed by the compressed air injected from the scarfing nozzle (29). To be configured.

上記のとおり構成したから、装炭車(3)が給炭ホッパ
ー(5)に図示しない石炭塔で装入炭を積載し、所定の
炭化室(4a)の装炭位置まで走行してきて停止し、図示
しない蓋取装置により装入蓋(6)を取外す。ついで装
入フード(9)の装炭口(11)上に降下せしめたのち、
スライドゲート(7)を開放し、各給炭ホッパー(5)
内の装入炭を図示しないテーブルフィーダーで切出し、
補助ホッパー(8)、移動スリーブ(9)を介して炭化
室(4a)内に装入する。そして装入炭の装入終了後にレ
ベラー(10)により上面がレベリングされる。その間、
すなわち前記炭化室(4a)の装入蓋(6)を取外すと同
時に、蓋取装置(19)によって前回装入した炭化室(4
b)の装入蓋(6)を取外す。ついで傾動モーター(3
3)により抽気孔開孔装置(20)を所定角度に傾動させ
る。そして上下駆動モーター(26)を駆動し、歯車(3
2)およびラック(24)を介して開孔部材(25)を下方
に移動させ、炭化室(4b)内に装入された装入炭中に挿
入する。その後直ちに上下駆動モーター(26)を逆転さ
せて開孔部材(25)を上端まで移動させれば、炭中に炭
化室(4b)の上部空間に通じるガス抽気孔(31)が形成
される。
Since it is configured as described above, the coal car (3) loads the coal on the coal feeding hopper (5) in a coal tower (not shown), travels to the carburizing position of the predetermined carbonization chamber (4a), and then stops. The charging lid (6) is removed by a lid removing device (not shown). Then, after dropping it onto the charging port (11) of the charging hood (9),
Open the slide gate (7), and each coal feeding hopper (5)
Cut out the charged coal inside with a table feeder (not shown),
It is loaded into the carbonization chamber (4a) through the auxiliary hopper (8) and the moving sleeve (9). After the charging of the charging coal is completed, the leveler (10) levels the upper surface. in the meantime,
That is, at the same time when the charging lid (6) of the carbonizing chamber (4a) is removed, the carbonizing chamber (4) previously charged by the lid removing device (19) is removed.
Remove the charging lid (6) from b). Then tilt motor (3
By 3), the bleed hole opening device (20) is tilted at a predetermined angle. Then, the vertical drive motor (26) is driven, and the gear (3
2) The hole member (25) is moved downward through the rack (24) and inserted into the charging coal charged in the carbonization chamber (4b). Immediately thereafter, if the vertical drive motor (26) is reversed to move the aperture member (25) to the upper end, a gas extraction hole (31) communicating with the upper space of the carbonization chamber (4b) is formed in the charcoal.

つぎに傾動モーター(33)により抽気孔開孔装置(20)
の傾動角度を変え、再び上下駆動モーター(26)を駆動
し、歯車(32)およびラック(24)を介して開孔部材
(25)を下方に移動させ、炭化室(4b)内に装入された
装入炭中に挿入する。その後直ちに上下駆動モーター
(26)を逆転させて開孔部材(25)を上端まで移動させ
ることを数回繰返せば、各装炭口から数本の抽気孔が形
成される。
Next, using the tilting motor (33), the bleed hole opening device (20)
The tilting angle of is changed, the vertical drive motor (26) is driven again, the aperture member (25) is moved downward via the gear (32) and the rack (24), and it is loaded into the carbonization chamber (4b). Inserted in the charged coal. Immediately thereafter, the vertical drive motor (26) is rotated in the reverse direction and the opening member (25) is moved to the upper end, which is repeated several times, so that several bleed holes are formed from each coal charging port.

そして再び蓋取装置(19)により装炭口(11)の装入蓋
(6)が装着される。その間は、当該炭化室(4b)の上
昇管(12)に設置された高圧安水ノズル(13)からは高
圧安水を噴射し、炭化室(4b)内を負圧に保持し、装炭
口(11)からの粉塵と火炎の噴出を防止する。
Then, the charging lid (6) of the coal charging port (11) is mounted again by the lid removing device (19). During that time, high-pressure ammonium hydroxide is injected from the high-pressure ammonium hydroxide nozzle (13) installed in the ascending pipe (12) of the carbonization chamber (4b) to maintain negative pressure in the carbonization chamber (4b) for carbonization. Prevent dust and flame from spouting from the mouth (11).

装炭作業が終了して装炭口の装入蓋(6)が装着される
と、装炭車(3)を石炭塔に移動させ、給炭ホッパー
(5)に装入炭を積込み、次ぎの所定の炭化室(4)ま
で移動し、同様の作業を行う。
When the charging operation is completed and the charging lid (6) of the charging port is installed, the charging vehicle (3) is moved to the coal tower, and the charging coal is loaded into the coal feeding hopper (5). The same work is performed by moving to a predetermined carbonization chamber (4).

これら一連の作業によって、炭化室(4)の各装炭口
(11)には、数本の炭化室上部空間と通じる抽気孔(3
1)が形成される。しかも、抽気孔(31)が形成される
位置は、低温の窯口部近傍、炉内低温部等窯毎の燃焼特
性に合せた位置に開孔することが可能であり、コークス
の均一乾留に寄与するところ大である。
As a result of these series of operations, each coal charging port (11) of the carbonization chamber (4) has a bleed hole (3
1) is formed. Moreover, the position where the extraction hole (31) is formed can be opened in the vicinity of the low temperature kiln mouth, the low temperature part in the furnace, etc. according to the combustion characteristics of each kiln, and for uniform dry distillation of coke. It is a great place to contribute.

実施例2 炉高7125mm、炉長16500mm、炉幅460mmのコークス炉にお
いて、平均フリュー温度1210℃、平均乾留時間22時間の
操業条件で、第1表に示す全水分9.2%の装入炭を実施
例1で説明した装炭車(3)を用いて装入し、その装炭
作業中に蓋取装置(19)で前回の装入炭化室(4b)の装
入蓋(6)を取外し、4ケの各装炭口(11)から傾斜角
度20゜で1装炭口あたり左右2本、炭中部に向かって直
径50mmの開孔部材(25)を開孔深度2mまで差込み、直ち
に開孔部材(25)を上昇させて炭化室上部空間に通じる
抽気孔(31)を設けた。
Example 2 In a coke oven having a furnace height of 7125 mm, a furnace length of 16500 mm, and a furnace width of 460 mm, charging coal having a total water content of 9.2% shown in Table 1 was carried out under the operating conditions of an average flue temperature of 1210 ° C. and an average carbonization time of 22 hours. Charging is performed by using the carburizing car (3) described in Example 1, and during the carburizing work, the capping device (19) is used to remove the charging cap (6) of the previous charging and carbonizing chamber (4b). From each coal charging port (11) at an inclination angle of 20 °, 2 holes on each side of the coal charging port, and a hole member (25) with a diameter of 50 mm toward the middle part of the coal is inserted up to a hole depth of 2 m, and the hole member is immediately opened. A bleed hole (31) was provided to raise (25) and communicate with the upper space of the carbonization chamber.

その間は、当該炭化室(4b)の上昇管(12)に設置され
た高圧安水ノズル(13)からは高圧安水を噴射し、炭化
室(4b)内を負圧に保持して装炭口(11)からの粉塵と
火炎の噴出を防止した。
In the meantime, high-pressure ammonium hydroxide nozzle (13) installed in the ascending pipe (12) of the carbonization chamber (4b) injects high-pressure ammonium hydroxide to maintain the inside of the carbonization chamber (4b) at a negative pressure for carbonization. Prevented dust and flame from spouting from the mouth (11).

このようにして傾動可能な抽気孔開孔装置(20)を設置
した装炭車(3)を使用し、炭化室(4b)に装入された
装入炭中に炭化室上部空間と通じる抽気孔(31)を設け
た場合のコークス炉の操業結果を、抽気孔を開孔しない
従来法1、各装炭口に垂直に1本の抽気孔を開孔した従
来法2と比較し、第2表に示す。
Using the coal car (3) equipped with the tilting bleed hole opening device (20), the bleed hole communicating with the upper space of the carbonization chamber during the charging of the carbonization chamber (4b). The operation results of the coke oven with (31) are compared with the conventional method 1 in which the extraction holes are not opened and the conventional method 2 in which one extraction hole is opened vertically to each charging port, Shown in the table.

第2表に示すとおり、本発明法の場合は、従来法2に比
較し抽気孔数が2倍であるが、装炭作業中に抽気孔開孔
作業が実施でき、装入作業総計内に占める開孔作業時間
は0秒であり、装炭作業には全く影響を与えなかった。
As shown in Table 2, in the case of the method of the present invention, the number of extraction holes is twice that in the conventional method 2, but the extraction hole opening work can be performed during the carbonization work, and The opening work time occupying was 0 seconds and had no effect on the carbonization work.

また、角度20゜で各装炭口に左右2本の抽気孔を設けた
本発明法の場合は、石炭中の温度が乾留の終了を示す90
0℃に達するまでの時間が、従来法1に比較し2時間短
縮され、従来法2に比較しても0.8時間短縮されてい
る。
Further, in the case of the method of the present invention in which each coal charging port is provided with two extraction holes on the left and right at an angle of 20 °, the temperature in the coal indicates the end of the carbonization.
The time required to reach 0 ° C. is shortened by 2 hours as compared with the conventional method 1 and 0.8 hours as compared with the conventional method 2.

このように本発明法では、石炭層内部に発生する水蒸気
量に対し十分な抽気能力を得ることができ、乾留終了ま
での所要時間が大幅に短縮されている。
As described above, according to the method of the present invention, a sufficient extraction capacity can be obtained for the amount of water vapor generated inside the coal seam, and the time required until the end of the carbonization is greatly shortened.

さらに注目すべきは、従来法2に比較して本発明法で
は、コークス強度が大幅に向上すると共に強度バラツキ
も明らかに大幅に低減している。これは、窯口近傍、低
温部の焼成遅れ部分への抽気孔の開孔により、その部分
の乾留が促進されたことによるものであり、本発明法が
コークス品質の安定向上に有効であることを示すもので
ある。
It should be further noted that, compared with the conventional method 2, the method of the present invention significantly improves the coke strength and also significantly reduces the strength variation. This is due to the fact that the dry distillation of the portion was promoted by the opening of the extraction hole in the vicinity of the kiln and the firing delay portion of the low temperature portion, and that the method of the present invention is effective in improving the stability of the coke quality. Is shown.

さらにまた本発明法は、第2表に示すとおり、乾留終了
したコークスを炭化室から押出し時の押出電流値が従来
法2よりもさらに小さく、コークスケーキの炉壁からの
肌離れが良好であることが明らかであり、炉壁保全の面
でも有効である。
Further, in the method of the present invention, as shown in Table 2, the extruding current value when extruding the coke after completion of the dry distillation from the carbonization chamber is smaller than that in the conventional method 2, and the skin separation of the coke cake from the furnace wall is good. It is clear that this is also effective in terms of wall protection.

実施例3 炉高5000mm、炉長14620mm、炉幅450mmで、炭化室の中央
上部装炭口間に低温部のあるコークス炉において、平均
フリュー温度1140℃、平均乾留時間21.5時間の運転条件
で、第3表に示す装入炭を用いて操業を行った。
Example 3 In a coke oven having a furnace height of 5000 mm, a furnace length of 14620 mm, a furnace width of 450 mm, and a low temperature portion between the central upper coal charging ports of the carbonization chamber, operating conditions of an average flue temperature of 1140 ° C. and an average carbonization time of 21.5 hours, Operation was carried out using the charged coal shown in Table 3.

低温部の両側の装炭口から垂直に抽気孔を開孔した従来
法と、左右から角度20゜で低温部近傍に抽気孔を開孔し
た本発明法のそれぞれについて、生成コークスの平均強
度と強度バラツキを測定した。その結果を第4表に示
す。
For each of the conventional method in which the extraction holes were opened vertically from the coal charging ports on both sides of the low temperature portion and the method of the present invention in which the extraction holes were opened in the vicinity of the low temperature portion at an angle of 20 ° from the left and right, the average strength of the generated coke and The strength variation was measured. The results are shown in Table 4.

第4表に示すとおり、窯の燃焼特性に合せて抽気孔を開
孔する本発明法は、コークス品質の安定と向上を図るこ
とができることが明らかである。
As shown in Table 4, it is clear that the method of the present invention in which the extraction holes are opened according to the combustion characteristics of the kiln can stabilize and improve the coke quality.

発明の効果 以上述べたとおり、この発明方法によれば、装炭口中心
を通る鉛直線を含む炉長方向断面内で、鉛直線に対し5
゜以上、40゜以下の角度で炭化室内の装入炭層中に抽気
孔を設けることにより、各装炭口毎に複数の抽気孔を開
孔することができ、石炭層内部に発生する水蒸気に対
し、十分な抽気能力を得ることができ、コークス化の促
進とコークス品質の安定向上、炉体保全に効果的であ
る。さらに、本発明装置は、鉛直線に対し5゜以上、40
゜以下の角度で各装炭口毎に複数本の抽気孔を、装炭作
業に何等支障を与えることなく開孔できる。
EFFECTS OF THE INVENTION As described above, according to the method of the present invention, in the furnace length direction cross section including the vertical line passing through the center of the coal charging port,
By providing bleed holes in the coal bed in the carbonization chamber at an angle of ≥40 ° and ≤40 °, it is possible to open multiple bleed holes for each coal inlet and On the other hand, a sufficient extraction capacity can be obtained, which is effective in promoting coking, stabilizing and improving coke quality, and maintaining the furnace body. In addition, the device of the present invention has
It is possible to open a plurality of bleeding holes for each carburizing port at an angle of ° or less without causing any trouble in the carburizing work.

そのうえ、本発明方法および装置は、窯口部付近、各窯
の燃焼特性に合せて、抽気孔位置を変更することも可能
であり、さらなるコークス品質の安定向上を図ることが
できる。
Moreover, the method and apparatus of the present invention can change the position of the bleed holes in accordance with the combustion characteristics of the kiln opening portion and each kiln, and can further improve the stability of coke quality.

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

第1図はこの発明の抽気孔開孔装置を供えた装炭車とコ
ークス炉の炉団方向の一部概略断面図、第2図は同じ装
炭車とコークス炉の炉長方向の一部概略断面図、第3図
は開孔部材を上下動する駆動手段を示す拡大図である。 1……コークス炉、2……レール、 3……装炭車、4……炭化室、 5……給炭ホッパー、6……装入蓋、 10……レベラー、11……装炭口、 12……上昇管、13……高圧安水噴射ノズル 19……蓋取装置、20……抽気孔開孔装置、 21、23……ガイドパイプ、 22……ガイドローラー、24……ラック、 25……開孔部材、26……上下駆動モーター、 27……上部センサー、28……下部センサー、 29……スカーフィングノズル、 30……架台、31……抽気孔、 32……歯車、33……傾動用モーター、
FIG. 1 is a partial schematic cross-sectional view of a coal car and a coke oven provided with a bleeding hole opening device of the present invention in the furnace group direction, and FIG. 2 is a partial schematic cross-section of the same car car and coke oven in the furnace length direction. FIG. 3 and FIG. 3 are enlarged views showing the driving means for moving the aperture member up and down. 1 ... Coke oven, 2 ... Rail, 3 ... Charging car, 4 ... Carbonization chamber, 5 ... Charging hopper, 6 ... Charging lid, 10 ... Leveler, 11 ... Charging port, 12 …… Rise pipe, 13 …… High pressure water spray nozzle 19 …… Lid removal device, 20 …… Bleed hole opening device, 21, 23 …… Guide pipe, 22 …… Guide roller, 24 …… Rack, 25… … Opening member, 26 …… Vertical drive motor, 27 …… Upper sensor, 28 …… Lower sensor, 29 …… Scarfing nozzle, 30 …… Stand, 31 …… Bleed hole, 32 …… Gear, 33 …… Tilting motor,

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】室炉式コークス炉の炭化室に装入された水
分を含む装入炭の表面から装入炭層中に炭化室上部空間
と通じる抽気孔を開孔する方法において、装炭口中心を
通る鉛直線を含む炉長方向断面内で、鉛直線に対し5゜
以上、40゜以下の角度で炭化室内の装入炭層中に1ない
し複数本の抽気孔を設けることを特徴とするコークス炉
装入炭の抽気孔開孔法。
Claim: What is claimed is: 1. A method for opening a bleed hole communicating with an upper space of a carbonization chamber from a surface of a coal containing water charged in a carbonization chamber of a chamber furnace type coke oven into a carbonization chamber upper space. One or more bleed holes are provided in the coal bed in the carbonization chamber at an angle of 5 ° or more and 40 ° or less with respect to the vertical line in the cross section of the furnace length direction including the vertical line passing through the center. Extraction hole opening method for charging of coke oven.
【請求項2】室炉式コークス炉の炭化室に装入された水
分を含む装入炭の表面から装入炭層中に炭化室上部空間
と通じる抽気孔を開孔する装置において、装炭位置に停
止した装炭車の前回の装炭窯位置に装入蓋蓋取装置、開
孔部材とその上下動駆動手段からなる抽気孔開孔装置お
よび該抽気孔開孔装置の傾動機構を設置したことを特徴
とするコークス炉装入炭の抽気孔開孔装置。
2. An apparatus for opening a bleeding hole communicating with an upper space of a carbonization chamber in a coal bed from a surface of a coal containing water charged in a carbonization chamber of a chamber furnace type coke oven. At the previous coal-charging kiln position of the coal-charging vehicle that stopped at that time, the charging-lid lid removing device, the bleed-hole piercing device including the piercing member and the vertical movement driving means, and the tilting mechanism of the bleed-hole piercing device are installed. The feature is a bleeder opening device for charging the coke oven.
JP28509690A 1990-10-22 1990-10-22 Extraction method and equipment for coke oven charging Expired - Fee Related JPH07100793B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28509690A JPH07100793B2 (en) 1990-10-22 1990-10-22 Extraction method and equipment for coke oven charging

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28509690A JPH07100793B2 (en) 1990-10-22 1990-10-22 Extraction method and equipment for coke oven charging

Publications (2)

Publication Number Publication Date
JPH04159391A JPH04159391A (en) 1992-06-02
JPH07100793B2 true JPH07100793B2 (en) 1995-11-01

Family

ID=17687079

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28509690A Expired - Fee Related JPH07100793B2 (en) 1990-10-22 1990-10-22 Extraction method and equipment for coke oven charging

Country Status (1)

Country Link
JP (1) JPH07100793B2 (en)

Also Published As

Publication number Publication date
JPH04159391A (en) 1992-06-02

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