JPS6011079Y2 - Coke charging device in coke dry fire extinguishing equipment - Google Patents

Coke charging device in coke dry fire extinguishing equipment

Info

Publication number
JPS6011079Y2
JPS6011079Y2 JP14184781U JP14184781U JPS6011079Y2 JP S6011079 Y2 JPS6011079 Y2 JP S6011079Y2 JP 14184781 U JP14184781 U JP 14184781U JP 14184781 U JP14184781 U JP 14184781U JP S6011079 Y2 JPS6011079 Y2 JP S6011079Y2
Authority
JP
Japan
Prior art keywords
coke
charging hopper
charging
cooling tower
extinguishing equipment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP14184781U
Other languages
Japanese (ja)
Other versions
JPS5848743U (en
Inventor
正栄 山口
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP14184781U priority Critical patent/JPS6011079Y2/en
Publication of JPS5848743U publication Critical patent/JPS5848743U/en
Application granted granted Critical
Publication of JPS6011079Y2 publication Critical patent/JPS6011079Y2/en
Expired legal-status Critical Current

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  • Coke Industry (AREA)

Description

【考案の詳細な説明】 本考案は、冷却塔内コークスの粒度偏析を減少させる、
コークス乾式消火設備におけるコークス装入装置に関す
る。
[Detailed description of the invention] The present invention reduces particle size segregation of coke in a cooling tower.
This invention relates to a coke charging device in coke dry extinguishing equipment.

第1図イ、口に示すごとく、赤熱コークスをコークス炉
aからパケットbに受骸するとき、該パケットb内に、
コークス炉側が細粒C□で反コークス炉側が粗粒C2の
粒度偏析が発生し、この粒度偏析は、コークス装入時に
、第2図に示すごとく、パケットb1装入ホッパーdを
介してそのまま冷却塔e内に持込まれ、細粒の部分は冷
却しにくく粗粒の部分は冷却しやすいという局部的な熱
交換性能のために、冷却塔eの冷却能力が著しく低下す
る。
As shown in Figure 1A, when red-hot coke is transferred from coke oven a to packet b, in packet b,
Particle size segregation occurs with fine particles C□ on the coke oven side and coarse particles C2 on the anti-coke oven side, and this particle size segregation is cooled as it is through the packet b1 charging hopper d when coke is charged, as shown in Figure 2. The cooling capacity of the cooling tower e is significantly reduced due to the local heat exchange performance in which the fine particles are difficult to cool while the coarse particles are easily cooled when brought into the tower e.

この粒度偏析を防止するには、例えば装入ホッパーを旋
回させ、冷却塔内に粗粒と細粒を円周方向上均一にばら
まけばよいが、従来のコークス装入装置には、コークス
全量を一旦装入ホツバーに受けるための手段がなかった
ので、パケットから装入ホッパーへコークス全量を排出
した後パケットが巻上げられ装入ホッパーから完全に離
れ装入ホッパーが旋回を開始するまでの間に、すでに相
当量のコークスが定位置のまま冷却塔内に落下してしま
っていた、従って、もし装入ホッパーを旋回させても、
粒度偏析はあまり減少しなかった。
To prevent this particle size segregation, for example, the charging hopper can be rotated to uniformly disperse coarse and fine particles in the circumferential direction within the cooling tower, but conventional coke charging equipment does not allow the total amount of coke to be Since there was no means to receive the coke into the charging hopper once, after the entire amount of coke was discharged from the packet to the charging hopper, the packet was hoisted up and completely separated from the charging hopper until the charging hopper started rotating. , a considerable amount of coke had already fallen into the cooling tower in place, so even if the charging hopper was rotated,
Particle size segregation was not significantly reduced.

一方、装入ホッパーを旋回させるためには、当然そのた
めの旋回装置が必要になり、該旋回装置の一部は、装入
ホッパー外に配置させる。
On the other hand, in order to rotate the charging hopper, a rotating device is naturally required, and a part of the rotating device is disposed outside the charging hopper.

従ってこの旋回装置を炉蓋開閉時に毎回移動させなけれ
ばならないが、これは装入装置自身を複雑なものとし合
理的でない。
Therefore, this rotating device must be moved every time the furnace lid is opened and closed, but this complicates the charging device itself and is not rational.

又、従来のコークス装入装置では、炉蓋を開く時、第3
図に示すごとく先ず炉蓋fを上方に持上げ、水封トラフ
gから炉蓋スカートhを脱出させ、その後水平移動させ
ていた。
In addition, in conventional coke charging equipment, when opening the furnace lid, the third
As shown in the figure, first the furnace lid f was lifted upward, the furnace lid skirt h was removed from the water seal trough g, and then it was moved horizontally.

つまり、従来のコークス装入装置では、炉蓋の上昇、下
降動作が不可欠であり、もし装入ホッパーを固定式とし
た場合、装入ホッパー下端と炉頂との間に、炉蓋の動作
のために余分な隙間を設けなければならなかった。
In other words, in conventional coke charging equipment, the raising and lowering operations of the furnace lid are essential, and if the charging hopper is fixed, there is a gap between the lower end of the charging hopper and the top of the furnace that controls the movement of the furnace lid. I had to create an extra gap for this.

この隙間は、装入時のコークス落下距離を大きくし、コ
ークスの粉化を増大させると共に、装入時の集塵作業の
邪魔になるものであった。
This gap increases the distance the coke falls during charging, increases the pulverization of coke, and obstructs the dust collection operation during charging.

本考案は斯かる観点に鑑み、上記不具合が生じることな
く粒度偏析を防止し得るコークス乾式消火設備における
コークス装入装置を提供することを目的としてなしたも
ので、炉頂に昇降自在な水封トラフを設置した冷却塔の
上部に、旋回自在な装入ホッパーを設け、該装入ホッパ
ー下部に開閉自在なゲートを設けたことを特徴とするも
のである。
In view of this, the present invention has been devised for the purpose of providing a coke charging device for coke dry extinguishing equipment that can prevent particle size segregation without causing the above-mentioned problems. The cooling tower is characterized in that a rotatable charging hopper is provided at the top of the cooling tower in which the trough is installed, and a gate that can be opened and closed is provided at the bottom of the charging hopper.

以下、本考案の実施例を図面に基いて説明する。Embodiments of the present invention will be described below with reference to the drawings.

冷却塔1の架構2にレール3を敷設し、該レール3上に
、炉蓋4を装置した炉蓋台車5を車輪6を介して載置し
、炉蓋4の周囲に炉蓋スカート7を取付けると共に炉蓋
台車5を、架構2上に配設した流体圧シリンダのごとき
炉蓋開閉装置8によってレール3に沿い走行させ得るよ
うにし、冷却塔1頂部に、流体圧シリンダのごとき水封
トラフ昇降装置9によって昇降し得るようにした水封ト
ラフ10を配設腰該水封トラフ10に伸縮継手11を取
付ける。
A rail 3 is laid on the frame 2 of the cooling tower 1, and a furnace lid cart 5 equipped with a furnace lid 4 is placed on the rail 3 via wheels 6, and a furnace lid skirt 7 is placed around the furnace lid 4. At the same time, the lid truck 5 can be moved along the rails 3 by a lid opening/closing device 8 such as a hydraulic cylinder arranged on the frame 2, and a water-sealed trough such as a hydraulic cylinder is installed at the top of the cooling tower 1. A water seal trough 10 that can be raised and lowered by a lifting device 9 is provided, and an expansion joint 11 is attached to the water seal trough 10.

上部架構12にリング状のレール13を敷設し、該レー
ル13上に車輪14を介して装入ホッパー15を載置し
、該装入ホッパー15をベベルギヤ16.17やモータ
18等から成る旋回駆動装置19により旋回し得るよう
にし、装入ホッパー15の下端に接続した補助ホッパー
20に、装入ホッパ−15下端開口部を塞ぎ得るようゲ
ート21を設ける。
A ring-shaped rail 13 is laid on the upper frame 12, and a charging hopper 15 is placed on the rail 13 via wheels 14. An auxiliary hopper 20 which can be rotated by the device 19 and is connected to the lower end of the charging hopper 15 is provided with a gate 21 so as to close the opening at the lower end of the charging hopper 15.

なお、図中22は赤熱コークス搬送用のパケット、23
は図示してない手段により左右同時に開閉し得るように
したパケットゲート、24は細粒の赤熱コークス、25
は粗粒の赤熱コークス、Aはコークス炉側、Bは反コー
クス炉側である。
In addition, in the figure, 22 is a packet for transporting red hot coke, and 23 is a packet for transporting red hot coke.
24 is a packet gate that can be opened and closed simultaneously on the left and right sides by a means not shown; 24 is fine red-hot coke; 25
is coarse-grained red-hot coke, A is on the coke oven side, and B is on the anti-coke oven side.

次に、本考案の作用について説明する。Next, the operation of the present invention will be explained.

コークス炉前で赤熱コークスを受骸したパケット22は
、図示してない巻上機により上限位置まで巻上げられ、
そのまま冷却塔1上部(炉頂)へ搬送される。
The packet 22 containing the red-hot coke in front of the coke oven is hoisted up to the upper limit position by a hoisting machine (not shown),
It is transported as it is to the upper part of the cooling tower 1 (furnace top).

この場合、第4図に示すごとくゲート21及び炉蓋4は
閉上し、水封トラフ10は上昇して炉蓋スカート7と協
働してシールがなされ、又旋回駆動装置19は停止して
いる。
In this case, as shown in FIG. 4, the gate 21 and the furnace lid 4 are closed, the water seal trough 10 is raised and cooperates with the furnace lid skirt 7 to form a seal, and the swing drive device 19 is stopped. There is.

冷却塔1上部に搬送されたパケット22は、巻上機によ
り所要位置まで下され、パケットゲート23が開かれて
赤熱コークスが全量装入ホッパー15に排出され、しか
る後室になったパケットは巻上機により巻上げられるが
、パケット22が装入ホッパー15に干渉しない位置ま
で上昇したら、水封トラフ昇降荘園9により水封トラフ
10は炉蓋スカート7と干渉しない位置まで下げられ、
旋回駆動装置19が駆動されて装入ホッパー15が旋回
を開始する。
The packets 22 transported to the upper part of the cooling tower 1 are lowered to a required position by a hoisting machine, the packet gate 23 is opened, and the entire amount of red-hot coke is discharged into the charging hopper 15. After that, the packets in the chamber are rolled up. Although it is hoisted by the upper machine, when the packet 22 rises to a position where it does not interfere with the charging hopper 15, the water seal trough 10 is lowered by the water seal trough lifting manor 9 to a position where it does not interfere with the furnace lid skirt 7,
The turning drive device 19 is driven and the charging hopper 15 starts turning.

装入ホッパー15が旋回を開始したら、同時に旋回開閉
装置8により炉蓋4が開かれ、その開動作が完了した後
ゲート21が開かれて装入ホッパー15内の粒度偏析の
ある赤熱コークスは、夫夫冷却塔1の全域にばらまかれ
る。
When the charging hopper 15 starts rotating, the furnace lid 4 is simultaneously opened by the rotating opening/closing device 8, and after the opening operation is completed, the gate 21 is opened and the red hot coke with particle size segregation in the charging hopper 15 is removed. Scattered over the entire area of Fufu Cooling Tower 1.

この結果、冷却塔1内のコークスの粒度偏析は減少する
As a result, the particle size segregation of coke in the cooling tower 1 is reduced.

赤熱コークスの落下が終了したら、次の装入に備えて装
入ホッパー15を定位置に停止させ、炉蓋4及びゲート
21をしめ、水封トラフ10を上昇させる。
When the red hot coke has finished falling, the charging hopper 15 is stopped at a fixed position in preparation for the next charging, the furnace lid 4 and gate 21 are closed, and the water seal trough 10 is raised.

これで装入の1サイクルが終了する。なお、本考案の実
施例では偏心してない装入ホッパーを使用する場合につ
いて説明したが、偏心ホッパーを採用すれば、一層大き
な粒度偏析減少効果が得られること、炉蓋開閉装置、水
封トラフ昇降装置としては流体圧シリンダのかわりにラ
ック−ピニオン等種々の手段を採用することができるこ
と、旋回駆動装置としてはベベルギヤに限らず、リング
ギヤーピニオン等種々の手段を採用することができるこ
と、その他、本考案の要旨を逸脱しない範囲内で種々変
更を加え得ること、等は勿論である。
This completes one charging cycle. In addition, in the embodiment of the present invention, the case where a charging hopper that is not eccentric is used has been explained, but if an eccentric hopper is adopted, an even greater effect of reducing particle size segregation can be obtained, and the furnace cover opening/closing device, water seal trough lifting and lowering The device can use various means such as a rack-pinion instead of a hydraulic cylinder, and the swing drive device is not limited to bevel gears, but can also use various means such as ring gear pinions. Of course, various changes may be made without departing from the gist of the invention.

本考案のコークス乾式消火設備におけるコークス装入装
置によれば、冷却塔内コークスの粒度偏析が減少するた
め、冷却塔の熱交換性能が上昇するという優れた効果を
奏し得る。
According to the coke charging device in the coke dry extinguishing equipment of the present invention, the particle size segregation of coke in the cooling tower is reduced, so it can have an excellent effect of increasing the heat exchange performance of the cooling tower.

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

第1図イ、口及び第2図はコークス乾式消火設備の説明
図、第3図はコークス乾式消火設備の冷却塔の炉蓋の付
近の説明図、第4図は本考案のコークス乾式消火設備に
おけるコークス装入装置の説明図、第5図は第4図の■
−■方向矢視図を示す。 図中1は冷却塔、7は炉蓋スカート、8は炉蓋開閉装置
、9は水封トラフ昇降装置、10は水封トラフ、15は
装入ホッパー 19は旋回駆動装置、21はゲートを示
す。
Figures 1 and 2 are explanatory diagrams of the coke dry extinguishing equipment, Figure 3 is an explanatory diagram of the vicinity of the furnace cover of the cooling tower of the coke dry extinguishing equipment, and Figure 4 is the coke dry extinguishing equipment of the present invention. Fig. 5 is an explanatory diagram of the coke charging device in Fig. 4.
−■ Shows a direction arrow view. In the figure, 1 is a cooling tower, 7 is a furnace lid skirt, 8 is a furnace lid opening/closing device, 9 is a water seal trough lifting device, 10 is a water seal trough, 15 is a charging hopper, 19 is a swing drive device, and 21 is a gate. .

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 炉頂に昇降自在な水封トラフを設置した冷却塔の上部に
、旋回自在な装入ホッパーを設け、該装入ホッパー下部
に開閉自在なゲートを設けたことを特徴とするコークス
乾式消火設備におけるコークス装入装置。
A coke dry extinguishing system characterized by having a charging hopper that can be rotated at the top of a cooling tower equipped with a water seal trough that can be raised and lowered at the top of the furnace, and a gate that can be opened and closed at the bottom of the charging hopper. Coke charging equipment.
JP14184781U 1981-09-24 1981-09-24 Coke charging device in coke dry fire extinguishing equipment Expired JPS6011079Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14184781U JPS6011079Y2 (en) 1981-09-24 1981-09-24 Coke charging device in coke dry fire extinguishing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14184781U JPS6011079Y2 (en) 1981-09-24 1981-09-24 Coke charging device in coke dry fire extinguishing equipment

Publications (2)

Publication Number Publication Date
JPS5848743U JPS5848743U (en) 1983-04-01
JPS6011079Y2 true JPS6011079Y2 (en) 1985-04-13

Family

ID=29934909

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14184781U Expired JPS6011079Y2 (en) 1981-09-24 1981-09-24 Coke charging device in coke dry fire extinguishing equipment

Country Status (1)

Country Link
JP (1) JPS6011079Y2 (en)

Also Published As

Publication number Publication date
JPS5848743U (en) 1983-04-01

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