JPH07119418B2 - Extraction method and equipment for coke oven charging - Google Patents

Extraction method and equipment for coke oven charging

Info

Publication number
JPH07119418B2
JPH07119418B2 JP33956789A JP33956789A JPH07119418B2 JP H07119418 B2 JPH07119418 B2 JP H07119418B2 JP 33956789 A JP33956789 A JP 33956789A JP 33956789 A JP33956789 A JP 33956789A JP H07119418 B2 JPH07119418 B2 JP H07119418B2
Authority
JP
Japan
Prior art keywords
charging
coal
coke oven
carbonization chamber
carbonization
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
JP33956789A
Other languages
Japanese (ja)
Other versions
JPH03197588A (en
Inventor
恵三 井上
邦彦 西岡
潔 三浦
孝文 佐地
幹夫 渡辺
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 JP33956789A priority Critical patent/JPH07119418B2/en
Publication of JPH03197588A publication Critical patent/JPH03197588A/en
Publication of JPH07119418B2 publication Critical patent/JPH07119418B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Coke Industry (AREA)

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中部に、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 the middle part of the coal containing the water charged in the carbonization chamber of a chamber-type 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原料炭は、両側の燃料室から炉壁を
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 coking coal charged in the carbonization chamber is indirectly heated from the fuel 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.

近時、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。例え
ば、乾留効率化を図るため通常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℃まで乾燥予熱して水分を2%以
下に低減する予熱炭装入法が実用化されている。
Recently, 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 oven body, and technological development for this purpose is underway. For example, in order to improve the efficiency of dry distillation, the total moisture content of the charged coal, which is normally 8-10%, is reduced to 5-6%, and the pre-heated dry coal is preheated to 170-250 ° C. Then, a preheated coal charging method for reducing the water content to 2% or less has been put into practical use.

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 to dry or preheat 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は採用されるに止ど
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 some coke plants are only adopted.

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、乾留効率化のために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, expansion of the furnace width or furnace height has been studied to improve the efficiency of dry distillation, but these are effective when a new coke oven is installed, but they cannot be applied to an existing coke oven, so the existing furnace is not applicable. It does not lead to the improvement of the efficiency of dry distillation.

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.

さらにまた、炉体延命対策として、近年補修技術が進歩
して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。また、炉体延命
のためには、炉温を下げて操業することが考えられる
が、これは生産性を下げてしまうため、乾留効率化とは
相矛盾した方法である。
Further, as a life extension measure for the furnace body, a repair technique has been advanced in recent years and has been greatly effective. This is a repair of a damaged furnace body and a post-treatment technique. Further, in order to extend the life of the furnace body, it is conceivable to lower the furnace temperature for operation, but this lowers the productivity and is a method contradictory to the improvement of the carbonization efficiency.

したがって、乾留効率化と炉体延命とを両立させなが
ら、コークス品質の安定向上を達成することは、極めて
難しい問題であった。
Therefore, it has been a very difficult problem to achieve stable improvement of coke quality while achieving both improvement of dry distillation efficiency and life extension of the furnace body.

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、水分を含有する装入炭
を乾留する際、乾留効率を低下させている原因が、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
り、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、炉壁から炭中部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内に差
込み、これを引抜くことにより炭化室上部空間部と通じ
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 pay attention to the dehydration behavior in the dry distillation process of the water content of 8 to 11% in the charging coal, and when the carbonization of the charging coal containing the water is carried out, the reason why the carbonization efficiency is lowered is There is a wall-side flow of steam generated in the coal bed at the initial stage of carbonization, and the flow can be 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). For example, it was confirmed that the heat transfer efficiency from the furnace wall to the middle part of the coal can be improved and the expansion pressure to the furnace wall can be suppressed. Then, after leveling the upper surface of the charging coal containing water charged in the carbonization chamber, the opening member is inserted into the coal in the furnace from the charging port on the furnace, and the upper part of the carbonization chamber is pulled out. It was clarified that a bleeding hole communicating with the 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.

コークス炉の炭化室に装入された装入炭中に、装入炭中
に含有される水分に基づく水蒸気を抽気するための抽気
孔を設ける方法としては、種々の方法が考えられるが、
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ある。しかしながら、装炭口から開
孔部材を石炭内に差込み、抽気孔を開孔する作業は、高
温、粉塵およびガスによる悪環境下の筋力作業であり、
常時入力で行うことは極めて困難で、機械的に抽気孔を
開孔することが要望されている。
Various methods are conceivable as a method for providing an extraction hole for extracting steam based on water contained in the charging coal during charging charging into the carbonization chamber of the coke oven,
The simplest method is to insert an opening member into the coal in the furnace from the charging port on the furnace and pull out. However, the work of inserting the opening member into the coal from the coal charging port and opening the extraction hole is a muscular work under a bad environment due to high temperature, dust and gas,
Since it is extremely difficult to always input data, it is required to mechanically open the extraction hole.

発明が解決しようとする課題 この発明は、上記要望に基づいてなされたもので、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、炭化室上部空間に炭中より抽気する抽気孔を、コー
クス炉の装炭作業中に開孔できるコークス炉装入炭の抽
気孔開孔法及び装置を提供するものである。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The present invention has been made based on the above-mentioned demand, and is a bleeding hole for bleeding steam or the like generated based on the water content of charged coal in the initial stage of carbonization from the coal into the upper space of the carbonization chamber. The present invention provides a bleeding hole opening method and apparatus for charging a coke oven, which can be opened during a coke oven charging operation.

課題を解決するための手段 本発明者らは、前記炭化室に装入された装入炭の炭中に
炭化室上部空間と通じる抽気孔を機械的に開孔するにつ
いて鋭意検討の結果、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いることに
着目し、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を付設することにより解決
できる。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が、装炭車の前回装入
窯位置に設置するから炉団方向端部に抽気孔開孔装置が
設置され、上下駆動機構を装炭口近傍に設置できるた
め、1本の開孔部材で抽気孔の開孔が可能となる。さら
に、抽気孔開孔装置を装炭作業のため停止した装炭車上
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。
Means for Solving the Problems The inventors of the present invention have earnestly studied about mechanically opening an extraction hole communicating with the upper space of the carbonization chamber in the coal of the charging coal charged in the carbonization chamber, and as a result, coke Focusing on the fact that the kiln removal work of the furnace is usually performed at 5 kiln pitches or several kiln pitches,
The problem can be solved by additionally providing a bleed hole opening device including a charging lid cover removing device, an opening member, and a vertical drive mechanism for the opening member. In addition, the upper end of the bleed hole opening device is restricted by the lower surface of the coal tower when the coal car is running, so it must be located below the upper end of the coal feeding hopper. Since the bleeding hole opening device is installed at the end portion in the furnace group direction and the vertical drive mechanism can be installed near the coal charging port, it is possible to open the bleeding hole with one opening member. Furthermore, since the bleed hole opening device is installed at the previous charging kiln position on the coal car that was stopped due to the carbonization work, the bleed hole opening work can be performed during the carbonization work.

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上昇管部
で実施されている高圧安水の噴射を継続し、炭化室内に
負圧に維持することにより解決できることを発明し、こ
の発明に到達した。
Regarding the problems of dust and flames ejected from the coal charging port during the bleeding hole opening work, the high-pressure ammonium water injection continued in the rising pipe to prevent dust generation during carbonization, and carbonization was continued. The inventors arrived at the present invention by inventing that the problem can be solved by maintaining a negative pressure in the room.

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上面から、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、開孔部材および該部材の上下駆動手段を設置
し、装炭作業中に前回装入窯の装入蓋を取外し、開孔部
材を上下駆動手段を介して装入炭層中に挿入、上昇せし
めたのち、装入蓋を装着するのである。
That is, the present invention relates to a method for opening a bleed hole communicating with an upper space of a carbonization chamber in a charging coal layer from an upper surface of a charging coal containing water charged in a carbonization chamber of a chamber furnace type coke oven. The charging lid lid removing device, the opening member and the vertical driving means of the member are installed at the previous charging furnace position of the coal charging car stopped at the position, and the charging lid of the previous charging furnace is removed during the carbonization work, The opening member is inserted into the charging coal layer through the vertical driving means and is raised, and then the charging lid is mounted.

また、炉室式コークス炉の炭化室に装入された水分を含
む装入炭の上面から、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、各装炭口に対応する装
入蓋蓋取り装置、開孔部材および該開孔部材の上下駆動
手段を設置したのである。
Also, in the device that opens the bleed hole that communicates with the upper space of the carbonization chamber in the coal bed from the upper surface of the coal containing water charged in the carbonization chamber of the furnace chamber type coke oven, stop at the carbonization position. In the previous coal-charging kiln position of the coal-charging vehicle, the charging lid lid removing device corresponding to each coal-charging port, the opening member, and the vertical driving means for the opening member are installed.

作用 この発明においては、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、開孔部材および該部
材の上下駆動手段を設置し、装炭作業中、前回装炭した
炭化室の装入蓋を蓋取装置により取外し、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
によって、装入炭中に水蒸気の抽気孔が開孔される。
Action In the present invention, the charging lid cover removing device, the opening member and the vertical driving means for the member are installed at the previous charging position of the coal-charging vehicle stopped at the coal-charging position. By removing the charging lid of the charred carbonization chamber with the lid removing device, and inserting the opening member into the charging charcoal through the vertical drive means and raising it, steam extraction holes are opened during charging charcoal. It

したがって、抽気孔開孔のために余分な作業時間を費
し、コークス炉の窯出し作業を遅延させることもない。
Therefore, extra work time is required for opening the bleed holes, 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)と抽気孔開孔装置
(20)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)
から構成されている。
Further, a lid removing device (19) for the charging lid (6) and a bleed hole opening device (20) are attached to the position of the previous charging / charging chamber of the coal charging vehicle (3) in the furnace group direction. This bleed hole opening device (20)
Includes a guide pipe (21), a guide roller (22), an aperture member (25) having a rack (24) supported by a lower guide pipe (23), a vertical drive motor (26), and an upper position sensor (27). ), Lower position sensor (28), scarfing nozzle (29) and pedestal (30) for aperture member (25)
It consists of

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)を装炭口(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(4b)
の装入蓋(6)を取外す。そして上下駆動モーター(2
6)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 the charging hood (9) onto the charging port (11),
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) performs leveling on the upper surface. In the meantime, that is, at the same time when the charging lid (6) of the carbonization chamber (4a) is removed, the carbonization chamber (4b) previously charged by the lid removing device (19).
Remove the charging lid (6). And the vertical drive motor (2
6) is driven to move the aperture member (25) downward through the gear (32) and the rack (24) and insert it 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.

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、各炭化室(4)には、装炭
口(11)の数だけ炭中に炭化室上部空間と通じる抽気孔
(31)が形成される。しかも、抽気孔(31)が形成され
る位置は、炭化室(4)のうちで最も嵩密度の高い装炭
口(11)の直下であるから、炉長方向のコークス化の均
一化に寄与するところ大である。
By these series of operations, the extraction holes (31) communicating with the upper space of the carbonization chamber are formed in the carbonization chamber (4) by the number of the charging ports (11). Moreover, since the position where the extraction hole (31) is formed is directly below the coal charging port (11) with the highest bulk density in the carbonization chamber (4), it contributes to uniform coking in the furnace length direction. It is a big place to do.

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)から装入炭
の炉幅方向中央部上面から、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 A coke oven having a furnace height of 7125 mm, a furnace length of 16500 mm and a furnace width of 460 mm was charged with coal having a total water content of 9.2% shown in Table 1 under the operating conditions of an average flue temperature of 1210 ° C. and an average dry distillation 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). 50mm in diameter from the top of the central part in the furnace width direction of the charging coal from each coal charging port (11) toward the middle part of the coal
The hole opening member (25) was inserted to a hole depth of 2 m, and the hole opening member (25) was immediately raised to provide an extraction hole (31) communicating 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、従来の操業結果と比較して第2
表に示す。
Using the coal car (3) thus equipped with the bleed hole opening device (20), the bleed hole (31) communicating with the upper space of the carbonization chamber during the charging of the carbonization chamber (4b). The result of coke oven operation with the provision of
Shown in the table.

第2表に示すとおり、本発明方法の場合は、装炭作業中
に前回装入炭化室の抽気孔開孔作業を実施するため、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い。
As shown in Table 2, in the case of the method of the present invention, since the bleeding hole opening work of the previous charging / charging chamber is performed during the charging operation, the opening work time in the total charging work is 0 seconds. Yes, it has no effect on coal charging work.

また、抽気孔開孔中も高圧安水の噴射を継続して炭化室
内を負圧に維持したため、大きな発塵はなく、従来方法
に比較して若干増加したが、操業には全く影響を与える
ものではなかった。
In addition, since the high-pressure low-pressure water was continuously injected during the opening of the bleed hole to maintain the negative pressure in the carbonization chamber, there was no large amount of dust generation, which was slightly increased compared to the conventional method, but it has no effect on the operation. It wasn't something.

このようにこの発明方法は、抽気孔開孔作業により装炭
作業に支障を与える問題は何等発生せず、有効な抽気孔
の開孔法である。
As described above, the method of the present invention is an effective method for opening the extraction holes without causing any problems that hinder the carbonization work by the extraction hole opening work.

また、コークス炉操業への影響は、本発明法の場合は、
900℃到達時間で1.2時間短縮されており、乾留促進効果
の大きいことが認められる。この結果コークスの乾留温
度も上がるため、ドラム強度が上昇し、そのバラツキも
低減してコークス品質の安定向上に有効である。さら
に、コークス押出し時の押出電流値も30アンペア低下し
ているから、乾留中の石炭膨脹圧力が低下し、コークス
ケーキの炉壁からの肌離れが十分に行なわれたものと推
定され、炉壁保全の面でも有効である。
Further, the influence on the operation of the coke oven, in the case of the method of the present invention,
The time required to reach 900 ° C was shortened by 1.2 hours, confirming that the effect of promoting carbonization is great. As a result, the carbonization temperature of the coke rises, the drum strength rises, and its variation is reduced, which is effective in stabilizing the coke quality in a stable manner. Furthermore, the extrusion current value during coke extrusion was also reduced by 30 amps, so the coal expansion pressure during carbonization was reduced, and it is estimated that the skin of the coke cake was sufficiently separated from the oven wall. It is also effective in terms of conservation.

発明の効果 この発明方法によれば、水分を含有する装入炭を室炉式
コークス炉で乾留時、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。しかも、装入炭
の炭中に炭化室上部空間と通じる抽気孔を、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 According to the method of the present invention, it is effective for promoting coke formation, stable improvement of coke quality, and maintenance of the furnace body during dry distillation of the charged coal containing water in the coke oven chamber furnace. Moreover, the bleeding holes communicating with the upper space of the carbonization chamber can be opened in the charcoal charged without causing any hindrance to the carbonization work.

【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、
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 ...
… Carburizing chamber, 5 …… Coating hopper, 6 …… Charging lid, 10 ……
Leveler, 11 …… Coaling port, 12 …… Rise pipe, 13 …… High pressure water spray nozzle, 19 …… Lid removing 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,

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐地 孝文 茨城県鹿島郡鹿島町大字光3番地 住友金 属工業株式会社鹿島製鉄所内 (72)発明者 渡辺 幹夫 茨城県鹿島郡鹿島町大字光3番地 住友金 属工業株式会社鹿島製鉄所内 (56)参考文献 特開 平1−198686(JP,A) 特開 平3−192191(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takafumi Saji, No.3, Hikari, Oshima, Kashima-machi, Kashima-gun, Ibaraki Prefecture, Sumitomo Metal Industries, Ltd., Kashima Steel Works (72) Mikio Watanabe, Otsuko, Oshima, Kashima-machi, Kashima-gun, Ibaraki Prefecture Address Sumitomo Kinzoku Kogyo Co., Ltd. Kashima Steel Works (56) Reference JP-A-1-198686 (JP, A) JP-A-3-192191 (JP, A)

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
分を含む装入炭の上面から、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、
開孔部材および該部材の上下駆動手段を設置し、装炭作
業中に前回装入窯の装入蓋を取外し、開孔部材を上下駆
動手段を介して装入炭層中に挿入、上昇せしめたのち、
装入蓋を装着す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 of opening a bleed hole communicating with an upper space of a carbonization chamber in a charging coal layer from an upper surface of a coal containing water charged in a carbonization chamber of a chamber coke oven. In the previous coal-charging kiln position of the coal-charging car that stopped at the position, the charging lid lid removing device,
An opening member and a vertical driving means for the member were installed, the charging lid of the previous charging kiln was removed during the coal charging operation, and the opening member was inserted into the charging coal layer through the vertical driving means and moved up. Later,
A bleed hole opening method for charging coal in a coke oven, which is equipped with a charging lid.
【請求項2】室炉式コークス炉の炭化室に装入された水
分を含む装入炭の上面から、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、各装炭口に対応
する装入蓋蓋取装置、開孔部材および該開孔部材の上下
駆動手段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 bleed hole communicating with an upper space of a carbonization chamber in a charging coal layer from an upper surface of a coal containing water charged in a carbonization chamber of a chamber furnace type coke oven. A coke oven characterized in that, at the previous coal-charging kiln position of the coal-charging vehicle stopped at the position, a charging-lid lid removing device corresponding to each coal-charging port, an opening member, and vertical driving means for the opening member are installed. Bleed hole opening device for charging coal.
JP33956789A 1989-12-26 1989-12-26 Extraction method and equipment for coke oven charging Expired - Fee Related JPH07119418B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33956789A JPH07119418B2 (en) 1989-12-26 1989-12-26 Extraction method and equipment for coke oven charging

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33956789A JPH07119418B2 (en) 1989-12-26 1989-12-26 Extraction method and equipment for coke oven charging

Publications (2)

Publication Number Publication Date
JPH03197588A JPH03197588A (en) 1991-08-28
JPH07119418B2 true JPH07119418B2 (en) 1995-12-20

Family

ID=18328695

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33956789A Expired - Fee Related JPH07119418B2 (en) 1989-12-26 1989-12-26 Extraction method and equipment for coke oven charging

Country Status (1)

Country Link
JP (1) JPH07119418B2 (en)

Families Citing this family (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7998316B2 (en) 2009-03-17 2011-08-16 Suncoke Technology And Development Corp. Flat push coke wet quenching apparatus and process
US9200225B2 (en) 2010-08-03 2015-12-01 Suncoke Technology And Development Llc. Method and apparatus for compacting coal for a coal coking process
IN2015KN00248A (en) 2012-07-31 2015-06-12 Suncoke Technology & Dev Llc
US9249357B2 (en) 2012-08-17 2016-02-02 Suncoke Technology And Development Llc. Method and apparatus for volatile matter sharing in stamp-charged coke ovens
US9359554B2 (en) 2012-08-17 2016-06-07 Suncoke Technology And Development Llc Automatic draft control system for coke plants
US9243186B2 (en) 2012-08-17 2016-01-26 Suncoke Technology And Development Llc. Coke plant including exhaust gas sharing
US9169439B2 (en) 2012-08-29 2015-10-27 Suncoke Technology And Development Llc Method and apparatus for testing coal coking properties
EP2898048B8 (en) 2012-09-21 2020-08-12 SunCoke Technology and Development LLC Reduced output rate coke oven operation with gas sharing providing extended process cycle
WO2014105065A1 (en) 2012-12-28 2014-07-03 Suncoke Technology And Development Llc. Vent stack lids and associated systems and methods
US10883051B2 (en) 2012-12-28 2021-01-05 Suncoke Technology And Development Llc Methods and systems for improved coke quenching
WO2014105063A1 (en) 2012-12-28 2014-07-03 Suncoke Technology And Development Llc. Systems and methods for maintaining a hot car in a coke plant
US9238778B2 (en) 2012-12-28 2016-01-19 Suncoke Technology And Development Llc. Systems and methods for improving quenched coke recovery
US9476547B2 (en) 2012-12-28 2016-10-25 Suncoke Technology And Development Llc Exhaust flow modifier, duct intersection incorporating the same, and methods therefor
US10047295B2 (en) 2012-12-28 2018-08-14 Suncoke Technology And Development Llc Non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods
US9273249B2 (en) 2012-12-28 2016-03-01 Suncoke Technology And Development Llc. Systems and methods for controlling air distribution in a coke oven
CN104902984B (en) 2012-12-28 2019-05-31 太阳焦炭科技和发展有限责任公司 System and method for removing the mercury in emission
US9193915B2 (en) 2013-03-14 2015-11-24 Suncoke Technology And Development Llc. Horizontal heat recovery coke ovens having monolith crowns
US9273250B2 (en) 2013-03-15 2016-03-01 Suncoke Technology And Development Llc. Methods and systems for improved quench tower design
EP3090034B1 (en) 2013-12-31 2020-05-06 Suncoke Technology and Development LLC Methods for decarbonizing coking ovens, and associated systems and devices
CA2954063C (en) 2014-06-30 2022-06-21 Suncoke Technology And Development Llc Horizontal heat recovery coke ovens having monolith crowns
UA123493C2 (en) 2014-08-28 2021-04-14 Санкоук Текнолоджі Енд Дівелепмент Ллк Method and system for optimizing coke plant operation and output
AU2015317909B2 (en) 2014-09-15 2020-11-05 Suncoke Technology And Development Llc Coke ovens having monolith component construction
US10975310B2 (en) 2014-12-31 2021-04-13 Suncoke Technology And Development Llc Multi-modal beds of coking material
US11060032B2 (en) 2015-01-02 2021-07-13 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
EP3240862A4 (en) 2015-01-02 2018-06-20 Suncoke Technology and Development LLC Integrated coke plant automation and optimization using advanced control and optimization techniques
CA3203921A1 (en) 2015-12-28 2017-07-06 Suncoke Technology And Development Llc Method and system for dynamically charging a coke oven
EP3465369A4 (en) 2016-06-03 2020-01-15 Suncoke Technology and Development LLC Methods and systems for automatically generating a remedial action in an industrial facility
WO2018217955A1 (en) 2017-05-23 2018-11-29 Suncoke Technology And Development Llc System and method for repairing a coke oven
WO2020140086A1 (en) 2018-12-28 2020-07-02 Suncoke Technology And Development Llc Particulate detection for industrial facilities, and associated systems and methods
WO2020140079A1 (en) 2018-12-28 2020-07-02 Suncoke Technology And Development Llc Decarbonizatign of coke ovens, and associated systems and methods
US11365355B2 (en) 2018-12-28 2022-06-21 Suncoke Technology And Development Llc Systems and methods for treating a surface of a coke plant
US11760937B2 (en) 2018-12-28 2023-09-19 Suncoke Technology And Development Llc Oven uptakes
BR112021012455B1 (en) 2018-12-28 2023-10-24 Suncoke Technology And Development Llc COKE OVEN
US11098252B2 (en) 2018-12-28 2021-08-24 Suncoke Technology And Development Llc Spring-loaded heat recovery oven system and method
US11395989B2 (en) 2018-12-31 2022-07-26 Suncoke Technology And Development Llc Methods and systems for providing corrosion resistant surfaces in contaminant treatment systems
CA3125585C (en) 2018-12-31 2023-10-03 Suncoke Technology And Development Llc Improved systems and methods for utilizing flue gas
CA3177017C (en) 2020-05-03 2024-04-16 John Francis Quanci High-quality coke products
WO2023081821A1 (en) 2021-11-04 2023-05-11 Suncoke Technology And Development Llc Foundry coke products, and associated systems, devices, and methods
US11946108B2 (en) 2021-11-04 2024-04-02 Suncoke Technology And Development Llc Foundry coke products and associated processing methods via cupolas

Also Published As

Publication number Publication date
JPH03197588A (en) 1991-08-28

Similar Documents

Publication Publication Date Title
JPH07119418B2 (en) Extraction method and equipment for coke oven charging
JP2914198B2 (en) Coking furnace coal charging method and apparatus
JPH07100794B2 (en) Extraction method and equipment for coke oven charging
US6596128B2 (en) Coke oven flue gas sharing
AU2002239860A1 (en) Coke oven flue gas sharing
CN1280199A (en) Start method for directly smelting technology
KR100195432B1 (en) High temperature refractory material applying apparatus for the wall of a coking chamber in a coke battery
JPH0798943B2 (en) Extraction method and equipment for coke oven charging
US2018664A (en) Coking of coals
CN2890049Y (en) Thermal-state tamping coke oven
WO2011107198A1 (en) Method and device for coking coal mixtures having high driving pressure properties in a "non-recovery" or "heat-recovery" coking oven
JPH07100793B2 (en) Extraction method and equipment for coke oven charging
JP2550792B2 (en) Method and apparatus for extraction and carbonization of coke oven charging coal
JP3610680B2 (en) Reduction method of carbon adhesion in coke oven carbonization chamber
JPH0798944B2 (en) Extraction method and equipment for coke oven charging
JP3016116B2 (en) Coal carbonization method
JPH0415291A (en) Apparatus for making gas-bleeding hole through coal charged to coke oven
CN220432710U (en) Coke oven coke guide head-tail coke water flushing recovery device
JPH08283723A (en) Production of coke for blast furnace
JPH0826325B2 (en) Method and apparatus for bleeding holes in raw coke charged to coke oven
JPH05214343A (en) Method for opening bleeding hole of discharged carbon in coke furnace and device therefor
JP2503614Y2 (en) Bleed hole opening device for charging of coke oven
JPH07113077A (en) Method for opening bleeding hole in coal charged in carbonization chamber and hole opening apparatus
JPH03287693A (en) Method and apparatus for providing bleed holes in charging coal of coke oven
JPH04270788A (en) Method for extracting gas from coal charged in coke oven and device therefor

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees