JPS6015487A - Leveler equipped with compacting device for upper layer coal in coke oven - Google Patents
Leveler equipped with compacting device for upper layer coal in coke ovenInfo
- Publication number
- JPS6015487A JPS6015487A JP12437183A JP12437183A JPS6015487A JP S6015487 A JPS6015487 A JP S6015487A JP 12437183 A JP12437183 A JP 12437183A JP 12437183 A JP12437183 A JP 12437183A JP S6015487 A JPS6015487 A JP S6015487A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- leveler
- leveller
- carbonization chamber
- bearing
- 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.)
- Pending
Links
Landscapes
- Coke Industry (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は水平室炉式コークス炉(以下コークス炉と言う
)に石炭類を装入する場合、炉頂部に有る装入車で重力
装入し押出機に設置して有るレベラーでレベリング作業
を行なうレベラーの構造に関するものである。[Detailed Description of the Invention] When charging coal into a horizontal chamber type coke oven (hereinafter referred to as coke oven), the present invention is capable of gravity charging using a charging car installed at the top of the furnace and installing it in an extruder. This relates to the structure of a leveler that performs leveling work.
コークス炉に石炭類を装入する場合に、炉頂部の装入車
に石炭’)”sQ を受け、コークスを押出して猪にな
った炭化室両側の炉蓋を装着し、炉頂部の装入口蓋を開
放して装入車よpA重力装入行ない機械側炉蓋上部のレ
ベラー口を開放して押出機に設置したレベラーで炭化室
上部を往復摺動させてレベリングする。発生したコーク
ス炉ガスを炭化室から排出するだめの発生ガス排出口を
炭化室全長にわたって形成し発生ガスを上昇管口から排
出すると共に石炭類の均一加熱を行なうために装入した
□石炭上部をレベリングし石炭類を乾留するが従来の重
力装入、及びレベリング作業、乾留方法には次のような
問題点が有る。When charging coal into a coke oven, the charging car at the top of the furnace receives the coal, pushes out the coke, and attaches the lids on both sides of the carbonization chamber. Open the pallet and carry out pA gravity charging from the charging car. Open the leveler port at the top of the furnace lid on the machine side and level the coke oven gas by sliding the upper part of the coking chamber back and forth with the leveler installed in the extruder. A generated gas discharge port is formed along the entire length of the carbonization chamber to discharge the generated gas from the riser pipe opening, and the upper part of the charged coal is leveled to uniformly heat the coal. Although carbonization is performed, the conventional gravity charging, leveling work, and carbonization methods have the following problems.
(1)炭化室内の装入炭嵩督度は一般的に下部が高く上
部及び装入口間が低い傾向を持っておりそのバラツ゛キ
が大きい。(1) The bulk of charged coal in the carbonization chamber generally tends to be high at the bottom and low at the top and between the charging ports, and there is a large variation.
(2)装入した石炭類は乾留過程で軟化溶融、固化収縮
の状態が変化し、炭化室内にその状態が同時に存在し軟
化溶融体が炭化室炉中中央で合致し再同化してコークス
となるが炭化室上部にス、−+9ンジ状コークスが生成
し、又炉巾方向中央部のコークス品質が他に比較して劣
っている。(2) During the carbonization process, the charged coal changes states of softening, melting, and solidification shrinkage, and these states simultaneously exist in the carbonization chamber, and the softened and molten material meets in the center of the carbonization chamber and is re-assimilated into coke. However, the coke-like coke was formed in the upper part of the carbonization chamber, and the quality of the coke in the central part in the oven width direction was inferior compared to other parts.
(3)装入した石炭類のコークス化が完了するまで炭化
室壁附近と炭化室炉巾方向中心部では大きな温度差が存
在し、この温度差のために石炭の受ける熱履歴が炭化室
の場所によって異なりこれがコークス品質に影響を及ぼ
している。(3) Until coking of the charged coal is completed, there is a large temperature difference between the wall of the coking chamber and the center of the coking chamber in the width direction, and this temperature difference causes the thermal history of the coal to change in the coking chamber. This affects coke quality, which varies by location.
以上の如く炭化室内での乾留の進行の度合はその位置に
よって異なっておりその原因は、乾留温度、装入炭の嵩
密度、炭化室壁附近と中央部の熱履歴の違いによるもの
と考えられ一1乾留の反応もまた違ったものでありそれ
が、コークス品質に影響を与えている。As mentioned above, the degree of progress of carbonization in the carbonization chamber differs depending on its location, and the causes are thought to be the carbonization temperature, the bulk density of the charged coal, and the difference in thermal history between the vicinity of the wall and the center of the carbonization chamber. The reaction of carbonization is also different, which affects coke quality.
この発明はかかる問題点に鑑みレベリング作業に於ける
装入炭の炭化室上部及び炉巾方向中央部の嵩密度を高め
それによってコークス品質の向上とそのバラツキ低減を
図るだめのレベラー全提供するものである。In view of this problem, the present invention provides a leveler that increases the bulk density of charged coal in the upper part of the coking chamber and in the center in the width direction of the furnace during leveling work, thereby improving the quality of coke and reducing its dispersion. It is.
すなわち本発明装置はレベラー先端部枠体に取付けて装
入した石炭類のレベリング作業に使用するものでコーク
ス炉炭化呈炉【1]方向の中央部に位置する如くレベラ
ー枠体の中央部にビンに依って回転目在なる如く取付け
られた圧密ローラーを有するリンクの他端を旋回可能な
![1く係合部によシ取付けられた袖ケ、レベラー枠体
内両側に設けたガイげに保合部を設けて上下動13J’
ii目な如く構成して取付けられた軸受に取付けると
共にその軸受の一端に保合部を設けた連板を出して、レ
ベラー枠体に軸で旋回可能な如く取伺けられた墾気又は
油圧シリンダーの一ノド先厨1h部が係合金物を介して
軸受連板に軸でシリンダーが旋回可能な如く取付けられ
ていて、コークス炉頂部の装入口から炭化室に装入され
た石炭類をレベリングする際に空気又は油圧シリンダー
を操作して圧管ローラーが最下部に位置することにより
ttil+受高さを調整し押出機側炉蓋の上部に位置す
るレベラー口を開放し、戻!ll辰娘送及び石炭類の)
1り敗防止のためにレベラー枠体下に取付けである移動
7−−トを炉蓋上部の窯内迄移動して設訂してレベラー
を炭化室内に進入させると先端に圧密ローラーを備えだ
リンクが窯内移動シーート先端部より外れた位置で圧+
80−ラ一部の重錘作用によシ下方に回転してレベラー
枠体に鉛直に位置し、更にレベラーを進入させると圧密
ローラーが回転しながら炉巾方向中央部の石炭類を押圧
しながらレベリングする。次にレベラーを後進させる際
にレベラー枠体に取付けである空気又は油圧シリンダー
を操作して圧密ローラーを支持している軸受を上部に移
動してレベラーを後進すると前に圧密ローラーで押圧さ
れた石炭類の上部にレベラーで掻き込まれた石炭類が入
っておシレベ2−の後進時に圧密ローラーで更に石炭を
下部に押圧する。レベリング完了後はレベラーを所定の
位置に引戻すと圧密ローラーを備えたリンクが移動シュ
ートの下部をガイげにして旋回して上部に位置しレベラ
ー枠体内に納まり他の附属設備との干渉もなく作業が遂
行できる。That is, the device of the present invention is used for leveling the coal charged by being attached to the frame at the tip of the leveler. The other end of the link can be pivoted with a compaction roller attached to the rotation point! [1] The sleeve piece attached to the engaging part and the retaining part on the brace provided on both sides of the leveler frame allow for vertical movement of 13J'.
The pressure or hydraulic pressure is attached to a bearing configured as shown in item ii, and a continuous plate with a retaining portion provided at one end of the bearing is provided so that the leveler frame can be pivoted around the shaft. The 1h section at the end of the cylinder is attached to a bearing plate via a metal alloy so that the cylinder can rotate around a shaft, and is used to level the coal charged into the carbonization chamber from the charging port at the top of the coke oven. When doing so, operate the air or hydraulic cylinder to position the pressure tube roller at the lowest position to adjust the ttil + receiving height, open the leveler port located at the top of the extruder side furnace cover, and return it! ll Tatsumusume delivery and coal)
In order to prevent damage, the movable shaft installed under the leveler frame is moved to the inside of the kiln at the top of the furnace lid, and when the leveler is advanced into the carbonization chamber, a compaction roller is installed at the tip. Pressure increases when the link is removed from the tip of the moving sheet in the kiln.
80-Ra rotates downward due to the action of a part of the weight and is positioned perpendicularly to the leveler frame, and when the leveler further advances, the consolidation roller rotates and presses the coal at the center in the width direction of the furnace. Level up. Next, when moving the leveler backward, operate the air or hydraulic cylinder attached to the leveler frame to move the bearing supporting the consolidation roller to the top, and when the leveler moves backward, the coal pressed by the consolidation roller in the front will be removed. Coal scraped by a leveler is placed in the upper part of the coal pile, and when the coal pile 2- moves backward, the coal is further pressed to the lower part by a compaction roller. After leveling is completed, when the leveler is pulled back to the specified position, the link equipped with the compaction roller pivots around the lower part of the moving chute and is located at the upper part, where it is housed within the leveler frame and does not interfere with other auxiliary equipment. Able to perform work.
このようにしてレベラーを往復摺動する毎に圧密ローラ
ーの高さを調贅しながら順次レベリングをする事により
装入された炭化室上部の石炭の嵩密度を高くすることが
出来、、 Ii+i便に乾留された上部コークスの品質
向上及び炉rlJ方向中央部のコークス品質の向上及び
バラツキの減少が可能となり良質コークスの生成が可能
となり、高密度向上により消費熱世の低減を図ることが
できその効果は極めて犬である。以下に本発明を図面に
示す実施例に基いて詳細にi況明する。In this way, by sequentially leveling while adjusting the height of the consolidation roller each time the leveler slides back and forth, the bulk density of the charged coal at the top of the carbonization chamber can be increased, It is possible to improve the quality of the upper coke carbonized in the furnace, improve the quality of the coke in the central part of the furnace rlJ direction, and reduce the dispersion, making it possible to produce high-quality coke. The effect is extremely canine. The present invention will be explained in detail below based on embodiments shown in the drawings.
第1図はコークス炉炭化室におけるレベリング開始直前
の本発明実施例装置の主要断面説明図、第2図はコーク
ス炉炭化室におけるレベリング初期の本発明実施例の主
要断面図、第3図はコークス炉炭化室におけるレベリン
グ後期の本発明実施例の主要断面図、第4図はレベリン
グ終了後の本発明実施例装置の生麦断面図、第5図は本
発明の装置説明図である。FIG. 1 is a main sectional explanatory view of the embodiment of the present invention immediately before the start of leveling in the coke oven carbonization chamber, FIG. 2 is a main sectional view of the embodiment of the present invention at the initial stage of leveling in the coke oven carbonization chamber, and FIG. 3 is a coke FIG. 4 is a main sectional view of the embodiment of the present invention in the latter stage of leveling in the furnace carbonization chamber, FIG. 4 is a sectional view of the raw barley apparatus of the embodiment of the present invention after leveling, and FIG. 5 is an explanatory diagram of the apparatus of the present invention.
第1図、第2図、第3図、第4図に示す如くコークス炉
蓋炭化室1の頂部2には装入口3が炉長方向に4ケ乃至
5ケ設催されておシ、そのコークス側及び押出機側の端
部には上昇管口4が設けてらシ各炭化室1に装入された
石炭’jt45よ多発生した=+ −クス炉ガス6は上
昇管口4を通りコレクチングメーン(図示省略)で捕集
され次工程へ送られる。コークス炉炭化室1の両側バッ
クステー7は炉体の炉長方向の炉締めを行っており窯口
部には炭化室1の天井部27から炉底部28にわたり炉
蓋枠8が数句けられていてコークス側炉薇9、と押出側
炉蓋で炭化室1が密閉されておシ押出側炉蓋10にはレ
ベリング用のレベラー口11と蓋12が装備されている
。炉頂部2には敷設された軌条(図示省略)上を装入車
(図示省略)が走行して各炭化室1に石炭類5を重力に
より装入し押出側炉蓋10のレベラー口11の蓋12を
開放し押出機に取付けた移動シュー)13を炉1M10
の上部まで進入させてレベラー14を往復摺1%bして
レベリングし、発生したコークス炉ガス6の排出口29
を確保し石炭類5の上部を均らして石炭類5を均一加熱
しレベリングにょシ余剰になった石炭類5は移動シーー
ト13と固定シュート15を経てホッパー15′に集め
て処理される。本発明の炭化室上部装入炭圧密装置を備
えたレベラー装置は第1図〜第4図に示す如くレベラー
14の先端部に取付けて使用する装置でc′J 5図に
示す如く圧密ロー216がビンJ7を介して回転自在な
如!
くリンク18の先端部に取付けられて抑圧部を構成しリ
ンク18の他端は軸19 ’に介してレベラー枠体20
の炉巾方向中央部に旋回[I任なる如く・曲受21にg
i[1立られている。軸受21はレベラー枠体20に溶
接によって取付けられたがイド金物22と凹型の保合部
を設けて上下動可能な如く取付られ更に軸受21の一端
に保合j$を有する7ランデ23が設けておシ、レベラ
ー枠体20に軸24で旋回n」能に数句けられた空気又
は油圧シリンダー25の接に完全1勿26と両1則の1
油受21を連結しているピア27とで回転自在なる如く
取付けられている。As shown in Fig. 1, Fig. 2, Fig. 3, and Fig. 4, four to five charging ports 3 are provided in the top part 2 of the coke oven lid carbonization chamber 1 in the furnace length direction. A riser pipe port 4 is provided at the ends of the coke side and the extruder side, so that the coke furnace gas 6 generated in excess of the coal charged in each carbonization chamber 1 passes through the riser pipe port 4 and is collected. It is collected by a cutting machine (not shown) and sent to the next process. The back stays 7 on both sides of the coke oven carbonization chamber 1 tighten the furnace body in the furnace length direction, and several furnace cover frames 8 are cut out at the furnace mouth from the ceiling 27 of the carbonization chamber 1 to the furnace bottom 28. The coking chamber 1 is sealed by a coke side furnace bell 9 and an extrusion side furnace lid, and the extrusion side furnace lid 10 is equipped with a leveler port 11 and a lid 12 for leveling. A charging car (not shown) runs on a rail (not shown) laid in the furnace top 2 to charge coal 5 into each carbonization chamber 1 by gravity, and then fills the leveler port 11 of the extrusion side furnace lid 10 with Open the lid 12 and move the moving shoe (13) attached to the extruder to the furnace 1M10.
The leveler 14 is leveled by reciprocating 1% b, and the discharge port 29 of the generated coke oven gas 6 is removed.
The upper part of the coal 5 is leveled, the coal 5 is heated uniformly, and the excess coal 5 passes through a moving sheet 13 and a fixed chute 15 and is collected in a hopper 15' for processing. The leveler device equipped with the coal compaction device charged at the top of the carbonization chamber of the present invention is a device that is attached to the tip of the leveler 14 as shown in FIGS. It looks like it can be rotated freely via bottle J7! The other end of the link 18 is connected to the leveler frame 20 via a shaft 19'.
Rotate in the center of the width direction of the furnace.
i[1 is set. The bearing 21 is attached to the leveler frame 20 by welding, and is attached so that it can move up and down by providing a concave retaining portion with the side metal fitting 22, and furthermore, a seven-runde 23 having a retainer is provided at one end of the bearing 21. Then, the air or hydraulic cylinder 25, which is rotated by the shaft 24 on the leveler frame 20, is connected to the leveler frame 20 with a complete 1 screw 26 and 1 of the 1 rule.
It is rotatably attached to a pier 27 that connects the oil pan 21.
本発明装置の使用例のび要はi:l)1図に示す如く炉
頂部2の装入車(図示省略)により炭化室lの各装入口
3よシ装入された石炭ジ、負5のレベリング作業は押出
側炉蓋10のレベラー口11の蓋12を開放して移動ゾ
z、−113を炭化室内炉蓋10の上部迄移動しレベラ
ー14を炭化室1内に進入させると第2図に示す如く装
置が移動シュート13の先端を外れた位置で圧密ローラ
ー16及びリンク18の自重による重錘作用で回転しレ
ベラー14の下方に位置する。更にレベラー14を進入
させると第3図に示す如くレベラーの移動につれて、圧
密ローラー16が回転しながらレベラー14の重みで炭
化室炉巾方向中央部石炭類5の上部を押圧しながらレベ
リングする。次に空気又は油圧シリンダー25を操作し
て軸受21を上部に移動させてレベリングすると今まで
押圧した石炭類5の上部にのった石炭類5を押圧しなが
らレベリングする。このように圧密ロー216の高さを
順次調整しレベラー枠体20の最上部まで軸受21を移
動させながらレベリングすることにょシ装入された石炭
類5の上部特に炉中中央の嵩密度が向上する。装入した
炭化室1の上部に発生したコークス炉ガス6の排出道を
造ってレベリング作業が完了すると第4図に示す如く空
気又は油圧シリンダー25を操作して軸受21の高さを
下方に移動しレベラー14を引抜くと移動シー−113
の先端部で圧密ローラ16とリンク18が上部に押し上
げられてレベラー枠体20内に納マリレベラー14を所
定の位置1fまで引き戻−j−ことが出来る。このよう
に本発明の炭化室上tJ装入炭圧密装置は炭化至上部特
に炉1↑J方向中火部の、”i’)’5 Ylff度を
++j、める事が出来それによってコークス品J・[の
向上とそのバラツキの減少が可能となり嵩密度向上によ
る消費熱量の1Js<減を図ることが出来る。An example of the use of the device of the present invention is i:l) 1) As shown in Figure 1, the coal charged through each charging port 3 of the carbonization chamber 1 by the charging car (not shown) in the furnace top 2 is The leveling work is performed by opening the lid 12 of the leveler port 11 of the extrusion-side furnace lid 10, moving the moving rod z, -113 to the upper part of the furnace lid 10 in the carbonization chamber, and moving the leveler 14 into the carbonization chamber 1, as shown in Fig. 2. As shown in FIG. 2, the device rotates under the weight action of the consolidation roller 16 and the link 18 at a position away from the tip of the movable chute 13 and is located below the leveler 14. When the leveler 14 is further advanced, as the leveler moves as shown in FIG. 3, the consolidation roller 16 rotates and levels the coals 5 in the widthwise center of the coking chamber while pressing the upper part of the coal 5 with the weight of the leveler 14. Next, by operating the air or hydraulic cylinder 25, the bearing 21 is moved upward for leveling, and the coal 5 placed on top of the previously pressed coal 5 is leveled while being pressed. In this way, by adjusting the height of the consolidation row 216 one after another and leveling while moving the bearing 21 to the top of the leveler frame 20, the bulk density of the charged coal 5 in the upper part, especially in the center of the furnace, is improved. do. When the leveling work is completed by creating a discharge path for the coke oven gas 6 generated in the upper part of the charged coke chamber 1, the height of the bearing 21 is moved downward by operating the air or hydraulic cylinder 25 as shown in Fig. 4. When the leveler 14 is pulled out, the moving seat 113
The compaction roller 16 and the link 18 are pushed upward at the tip of the leveler frame 20, and the leveler 14 can be pulled back to a predetermined position 1f. In this way, the above-charging coal compaction device of the present invention can increase the "i')'5 It is possible to improve J·[ and reduce its variation, and it is possible to reduce the amount of heat consumed by <1 Js by improving the bulk density.
第1図はコークス炉炭化室におけるレベリング開始直前
の不発り]実施例装置の主要1υi面説明図、第2図は
コークス炉炭化室におけるレベリング初期の本発明実施
911装置のよg:1新面説明図、第3図はコークス炉
炭化室におけるレベリング後期の本発明実施例装置:t
の主決断面説1.lIJ図、第4図はレベリングA(6
了後の不発り」実施例装置の主要断面説明図、第5図(
a) 、 (b) 、 (c) 、 (d)は本発明の
装置説明図である。図中
1・・・炭化室 2・・・炉頂部
3・・・装入口 4・・・上昇管口
5゛°石炭顛 6・・・コークス炉蓋スフ・・バックス
テー 8・・炉蓋枠
9・・・コークス側炉蓋 10・・押出俳;側炉(1f
11・・・レベラー「1 12・・・レベラー蓋13・
・・移動シュート 14・・・レベラー15・・・固定
シュー1−’15’・・・ホッパー16・・・圧密ロー
ラー 17・・・ピン1 8 ・・・ リ ン り 1
9 ・・・ I)山20・・・レベラー枠体 21・
・・軸受22・・・ガイド金物 23・・・フランジ部
24・・軸
25・・・空気又は油圧シリンダー
26・・・炭化室天井 27・・・炭化室炉底28・・
・コークス炉ガス排出口
第5 l11
((Z)
第5図
(C)
ノ乙Fig. 1 is an explanatory diagram of the main 1υi side of the embodiment device (misfire just before the start of leveling in the coke oven carbonization chamber), and Fig. 2 is the g:1 new side of the 911 device according to the present invention at the initial stage of leveling in the coke oven carbonization chamber. Explanatory diagram, Figure 3 is the apparatus according to the present invention in the latter stage of leveling in the coke oven carbonization chamber: t
Principal decision surface theory 1. lIJ diagram, Figure 4 shows leveling A (6
"Failure to occur after termination" Main cross-sectional explanatory diagram of the example device, Fig. 5 (
a), (b), (c), and (d) are explanatory diagrams of the apparatus of the present invention. In the figure: 1... Carbonization chamber 2... Furnace top 3... Charging port 4... Rising pipe opening 5゛° Coal frame 6... Coke oven lid backstay 8... Furnace lid frame 9...Coke side furnace lid 10...Extrusion pipe; side furnace (1f
11...Leveler "1" 12...Leveler lid 13.
...Moving chute 14...Leveler 15...Fixed shoe 1-'15'...Hopper 16...Consolidation roller 17...Pin 1 8...Ring 1
9...I) Mountain 20...Leveler frame 21.
... Bearing 22 ... Guide hardware 23 ... Flange portion 24 ... Shaft 25 ... Air or hydraulic cylinder 26 ... Carbonization chamber ceiling 27 ... Carbonization chamber hearth bottom 28 ...
・Coke oven gas outlet No. 5 l11 ((Z) Figure 5 (C) No.
Claims (1)
く枢着された軸受に、連結板の1端に回転自在なローラ
ーが係合転子で係合されていてその連結板の他端に設け
た保合部が軸で枢着されていると共にレベラー枠体に保
合転子で旋回自在に取付けられた空気又は油圧シリンダ
ーのピストン杆に枢着連結金物の保合部が、軸受の1端
に設けた連結部と係合転子で係合してレベラー枠体内先
端部に納められていることを特徴としたコークス炉装入
炭上部の圧密装置を備えたレベラー装置。A rotatable roller is engaged with one end of the connecting plate by an engagement trochanter, and a rotatable roller is installed on the other end of the connecting plate, on a bearing that is pivotally mounted to allow the guide installed in the leveler frame to move up and down. The retaining part of the piston rod of the air or hydraulic cylinder, which is pivotably attached to the leveler frame by a retaining rotor, is attached to one end of the bearing. 1. A leveler device equipped with a compaction device for the upper part of coal charged in a coke oven, characterized in that the device is engaged with a connecting portion provided in a coke oven by an engaging trochanter and is housed in a distal end portion of a leveler frame body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12437183A JPS6015487A (en) | 1983-07-08 | 1983-07-08 | Leveler equipped with compacting device for upper layer coal in coke oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12437183A JPS6015487A (en) | 1983-07-08 | 1983-07-08 | Leveler equipped with compacting device for upper layer coal in coke oven |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6015487A true JPS6015487A (en) | 1985-01-26 |
Family
ID=14883740
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12437183A Pending JPS6015487A (en) | 1983-07-08 | 1983-07-08 | Leveler equipped with compacting device for upper layer coal in coke oven |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6015487A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02215891A (en) * | 1989-02-16 | 1990-08-28 | Sumitomo Metal Ind Ltd | Method for forming groove for degassing of coking coal charge in coke oven |
| KR100508509B1 (en) * | 2000-12-22 | 2005-08-17 | 주식회사 포스코 | An apparatus for controlling automatically level of coal in coking chamber of coke oven |
| KR100748124B1 (en) * | 2001-09-11 | 2007-08-10 | 주식회사 포스코 | Load leveling and filling equipment for direct vehicles |
| KR100784133B1 (en) | 2006-12-18 | 2007-12-12 | 주식회사 포스코 | Leveler system of coke oven |
-
1983
- 1983-07-08 JP JP12437183A patent/JPS6015487A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02215891A (en) * | 1989-02-16 | 1990-08-28 | Sumitomo Metal Ind Ltd | Method for forming groove for degassing of coking coal charge in coke oven |
| KR100508509B1 (en) * | 2000-12-22 | 2005-08-17 | 주식회사 포스코 | An apparatus for controlling automatically level of coal in coking chamber of coke oven |
| KR100748124B1 (en) * | 2001-09-11 | 2007-08-10 | 주식회사 포스코 | Load leveling and filling equipment for direct vehicles |
| KR100784133B1 (en) | 2006-12-18 | 2007-12-12 | 주식회사 포스코 | Leveler system of coke oven |
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