JPH0364392A - Split charging method for coke dry fire extinguishing system cooling tower - Google Patents

Split charging method for coke dry fire extinguishing system cooling tower

Info

Publication number
JPH0364392A
JPH0364392A JP1200880A JP20088089A JPH0364392A JP H0364392 A JPH0364392 A JP H0364392A JP 1200880 A JP1200880 A JP 1200880A JP 20088089 A JP20088089 A JP 20088089A JP H0364392 A JPH0364392 A JP H0364392A
Authority
JP
Japan
Prior art keywords
coke
cooling tower
damper
bucket
red
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
Application number
JP1200880A
Other languages
Japanese (ja)
Inventor
Susumu Matsumura
進 松村
Tamefumi Ebihara
海老原 為文
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP1200880A priority Critical patent/JPH0364392A/en
Publication of JPH0364392A publication Critical patent/JPH0364392A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Coke Industry (AREA)

Abstract

PURPOSE:To make the amt. of coke storage uniform in a plurality of cooling towers and to thereby make the amt. of steam generation in a waste heat boiler uniform by keeping a damper at an intermediate degree of opening to leave a part of a red-hot coke and feeding it into another cooling tower in feeding the red-hot coke in a coke bucket into the cooling tower. CONSTITUTION:When a red-hot coke in a coke bucket is fed into a cooling tower of a plurality of cooling towers of a dry type coke quench apparatus, feeding of the coke is performed for a specified time while a damper of the coke bucket is kept at an intermediate degree of opening (e.g. feeding at an opening of 1/2 for 6sec) and the damper is closed while a part of the coke is left. The remaining coke is then fed into another cooling tower.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、複数の冷却塔のコークス保有量の均一かを
図り、廃熱ボイラーの蒸気発生量均一化を図るためのコ
ークス乾式消火装置冷却塔への分割装入方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] This invention is a coke dry fire extinguishing system cooling system for equalizing the amount of coke held in a plurality of cooling towers and equalizing the amount of steam generated from waste heat boilers. This article relates to a method of dividing charging into a column.

[従来の技術] コークス炉では、第3図においてコークス炉20から窯
出しした赤熱コークスを、コークカー21に積載したコ
ークバケット6に収容し、走行レール22上を走行して
コークス乾式消化装置(CDQと略称)23に運搬し、
CDQ23にコークバケット6の赤熱コークスを装入し
、CDQ23に吹き込まれる冷却ガスにより消化し、高
温となった冷却ガスを廃熱ボイラー(図示せず)に導き
熱回収するいわゆる赤熱コークスの乾式消化が行われて
いる。コークバケット6による赤熱コークスのCDQ2
3への装入は次のように行われている。第2図(A)に
おいてコークカーのコークバケット6をクレーン1の巻
上げドラム2で巻上げCDQ23の冷却塔上部ホッパー
12の上方にもたらし、第211ffl(B)に示すよ
うに、吊りビーム4を巻下げてコークバケット6の底部
をバゲット受は部11に着底させる。更に、巻卸してゆ
きダンパー9を全開し、パケットの赤熱コクス全量(約
28T)を冷却塔に装入する。全開してから装入が完了
するまでの所要時間は6秒である。第3図に示ずように
コー2バケット1台当たり2基の冷却塔がある場合でも
、上述のように1台の冷却塔にパケット内コークス全量
を装入していた。
[Prior Art] In a coke oven, red-hot coke discharged from a coke oven 20 in FIG. (abbreviated as) 23,
Red-hot coke from coke bucket 6 is charged into CDQ23, and it is extinguished by the cooling gas blown into CDQ23, and the high-temperature cooling gas is guided to a waste heat boiler (not shown) for heat recovery. It is being done. CDQ2 of red hot coke by coke bucket 6
The charging to No. 3 is carried out as follows. In FIG. 2(A), the coke bucket 6 of the coke car is hoisted by the hoisting drum 2 of the crane 1 and brought above the cooling tower upper hopper 12 of the CDQ23, and as shown in No. 211ffl (B), the hanging beam 4 is lowered. The bottom of the coke bucket 6 is brought into contact with the baguette holder 11. Furthermore, unwinding is continued, the damper 9 is fully opened, and the entire amount of red-hot gas in the packet (approximately 28 T) is charged into the cooling tower. The time required from fully opening to completing charging is 6 seconds. Even when there are two cooling towers per coke 2 bucket as shown in FIG. 3, the entire amount of coke in the packet is charged into one cooling tower as described above.

[発明が解決しようとする課題] 従来の装入方法のように、冷却塔にパケット内の赤熱コ
ークス全量を排出する方法では、複数の冷却塔を有する
場合、一つの冷却塔のコークス保有量の変動が大きくな
るために付属の廃熱ボイラーの蒸気発生量の変動が大き
くなり、且つ冷却塔間のコークス保有量にアンバランス
が生じ、付属する廃熱ボイラー間の蒸気発生量が不均一
となる。また、コークス乾式消火装置の修理のため、冷
却塔のコークス払出しに長時閏要するといった問題点が
あった。
[Problems to be Solved by the Invention] In the conventional charging method, in which the entire amount of red-hot coke in the packet is discharged into the cooling tower, when there are multiple cooling towers, it is difficult to reduce the amount of coke held in one cooling tower. As the fluctuation increases, the fluctuation in the amount of steam generated by the attached waste heat boiler increases, and an imbalance occurs in the amount of coke held between the cooling towers, resulting in unevenness in the amount of steam generated between the attached waste heat boilers. . Another problem was that it took a long time to remove coke from the cooling tower in order to repair the coke dry fire extinguishing system.

[課題を解決するための手段] この発明は上記のような問題点を解決しようとするもの
で、複数のコークス乾式消化装置一つの冷却塔に、コー
クバッケトの赤熱コークスを装入するに際し、コークバ
ケットのダンパーを途中開度に維持して、所定時間装入
し、コークバケット内にコークスの一部を残してダンパ
ーを全閉とし、残りのコークスを他の冷却塔に装入する
ことを特徴とするコークス乾式消火装置冷却塔への分割
装入方法である。
[Means for Solving the Problems] The present invention attempts to solve the above-mentioned problems, and when charging red-hot coke in a coke bucket to a cooling tower of a plurality of coke dry digesters, the coke bucket The damper is kept partially open and charged for a predetermined period of time, the damper is fully closed leaving a part of the coke in the coke bucket, and the remaining coke is charged to other cooling towers. This is a method of dividing coke into a dry coke extinguishing system cooling tower.

[作用] コークバケットの赤熱コークスを装入する際、ダンパー
を例えば1/2開とし6秒間(従来の全開排出時間)排
出後、ダンパーを閉じると約14Tをパケット内に残る
。この残りの14Tを他の冷却塔に装入するといった運
用ができる。
[Function] When charging red hot coke into a coke bucket, the damper is opened, for example, by 1/2, and after being discharged for 6 seconds (conventional fully open discharge time), when the damper is closed, about 14T remains in the packet. This remaining 14T can be used to charge other cooling towers.

従って冷却塔間の赤熱コークス保有レベルのバラツキお
よび各冷却塔の赤熱コークスの保有レベルの変動等を小
さくできる。
Therefore, variations in the level of red hot coke held between cooling towers and fluctuations in the level of red hot coke held in each cooling tower can be reduced.

[実施例コ 本発明の実施例を以下に詳細に説明する。第1図は本発
明の詳細な説明図である。1は第3区に示す冷却塔23
のそばのターンテーブル24および冷却塔の上方を移動
可能なりレーン、2は巻上げドラム、4は吊りビーム、
5は吊りビームの下の取り付けられた吊りフック、7は
コークバケット6の吊りロッド、8はダンパー開閉リン
ク連結金具である。9はダンパー、1oはダンパー開閉
用リンク、11はコークバケット6の荷重を受けるパケ
ット受は部である。
[Example] Examples of the present invention will be described in detail below. FIG. 1 is a detailed explanatory diagram of the present invention. 1 is the cooling tower 23 shown in the third section
2 is a winding drum, 4 is a hanging beam,
5 is a hanging hook attached under the hanging beam, 7 is a hanging rod of the coke bucket 6, and 8 is a damper opening/closing link connecting fitting. 9 is a damper, 1o is a link for opening and closing the damper, and 11 is a packet receiver that receives the load of the coke bucket 6.

コークバケット6の赤熱コークスを冷却塔に装入するに
は従来衣のように行っている。まず。
The red-hot coke from the coke bucket 6 is charged into the cooling tower in the same way as conventional methods. first.

コークカー21で冷却塔そばのターンテーブル24に運
搬してきたコークバケット6をクレーン1で吊上げ冷却
塔の上方にもたらす、クレーン1の巻上げドラム2を巻
下げ、コークバケット6の底部を冷却塔の上部に設けら
れたパケット受は部11に支持させる。この時点まで、
コークバケット6のダンパー9は吊りロッドがクレーン
フック5により吊上げられているので、ダンパー(両開
きダンパー)9は、吊りロッド7およびダンパ開閉用リ
ンク10を介して全開となっている。更に、巻上げドラ
ム2を巻下げると、吊りロッド7すなわちリンク連結金
具8が下がりダンパー9は、その支軸13の周りに回動
して開いて、パケット内の赤熱コークスが冷却塔に装入
される。
The coke bucket 6 transported by the coke car 21 to the turntable 24 near the cooling tower is lifted by the crane 1 and brought to the top of the cooling tower.The hoisting drum 2 of the crane 1 is lowered and the bottom of the coke bucket 6 is placed at the top of the cooling tower. The provided packet receiver is supported by part 11. Up until this point,
The suspension rod of the damper 9 of the coke bucket 6 is lifted by the crane hook 5, so the damper (double-opening damper) 9 is fully opened via the suspension rod 7 and the damper opening/closing link 10. Further, when the hoisting drum 2 is lowered, the hanging rod 7, that is, the link connecting fitting 8 is lowered, and the damper 9 rotates around its support shaft 13 and opens, and the red-hot coke in the packet is charged into the cooling tower. Ru.

28Tコークパケツトでは全閉から全開までの巻下げ量
は1400 am (Δh)であり、パケット内の赤熱
コークス全量の排出に要するは約6秒である。
In a 28T coke packet, the amount of lowering from fully closed to fully open is 1400 am (Δh), and it takes about 6 seconds to discharge the entire amount of red-hot coke in the packet.

本発明の方法は、コークバケット6の底部を冷却塔の上
部に設けられたパケット受は部11に支持させた後の巻
下げ量を従来の全開までの巻下げ量よりも少なくして、
ダンパー9を途中間とし、従来の全量排出時間排出後、
巻上げドラムを巻上げ排出を中止する。かくすれば、バ
ク゛ット内の赤熱コークスは全量排出されずコークバケ
ット6の中に赤熱コークスが残る。この残った赤熱コー
クスと他の冷却塔に装入するものである0例えば、上記
の28Tコークパケツトでは、パケットが受は部11に
支持された後の巻下げ量 Ah (ht−h2)=1.000mmとしくこのとき
の開度は半開となる)、6秒間排出して巻上げ全閉とす
る。このときのパケット内赤熱コークスの残量は約14
Tであった。この約147を他の冷却塔に装入する。こ
のようにすれば、2基の冷却塔のコークス保有量の変動
を小さくできる。
The method of the present invention reduces the lowering amount after the bottom of the coke bucket 6 is supported by the packet receiver 11 provided at the top of the cooling tower than the conventional lowering amount until fully opened.
After discharging the damper 9 for the conventional full discharge time,
Hoist the hoist drum and stop discharging. In this way, all of the red hot coke in the bucket is not discharged and the red hot coke remains in the coke bucket 6. This remaining red-hot coke is charged to other cooling towers.For example, in the above 28T coke packet, the amount of unwinding after the packet is supported by the receiving part 11Ah (ht-h2)=1. 000mm and the opening at this time will be half open), then discharge for 6 seconds and wind up to fully close. At this time, the remaining amount of red hot coke in the packet is approximately 14
It was T. Approximately 147 of this amount is charged to another cooling tower. In this way, fluctuations in the amount of coke held in the two cooling towers can be reduced.

巻下げ量Ahは、巻上げ装置等に組み込まれたリミット
スイッチの設定変更により行う、なお、冷却塔が3基の
ときは、巻下げ量Δhを変更し、ダンパー開度を1/3
開とし6秒間排出後ダンパーを全閉すればよい。
The lowering amount Ah is determined by changing the setting of the limit switch built into the hoisting device, etc. When there are three cooling towers, the lowering amount Δh is changed and the damper opening degree is set to 1/3.
Simply open the damper for 6 seconds, then fully close the damper.

[発明の効果] 本発明の方法は、以上のように構成されているから、冷
却塔が複数基ある場合、各冷却塔間の赤熱コークスの保
有レベルのバラツキを小さくでき、また各冷却塔のコー
クスの保有レベル変動を小さくできるから、廃熱ボイラ
ー間の蒸気発生量のバラツキおよび各廃熱ボイラーの蒸
気発生量の変動を小さくできる。また、コークス乾式消
火装置の修理のための冷却塔のコークス払出しに要する
時間を短くできるという効果が得られる。
[Effects of the Invention] Since the method of the present invention is configured as described above, when there are a plurality of cooling towers, it is possible to reduce the dispersion in the level of red-hot coke held between each cooling tower, and to reduce the variation in the level of red-hot coke held in each cooling tower. Since fluctuations in the coke retention level can be reduced, fluctuations in the amount of steam generated between waste heat boilers and fluctuations in the amount of steam generated by each waste heat boiler can be reduced. Further, an effect can be obtained in that the time required for discharging coke from a cooling tower for repairing a coke dry fire extinguishing system can be shortened.

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

第1図は本発明の詳細な説明図、第2図(A)(B)は
従来の装入方法の説明図、第3図はコクス炉におけるコ
ークス乾式消火装置の配置を示す図である。 1・・・クレーン、2・・・巻上げドラム、4−・・吊
りビーム、5・・・吊りフック、6・・・コークバゲッ
ト、7・・・吊りロッド、8・・・開閉リンク連結金具
、9・・・ダンパー10・・・ダンパー開閉リンク、 11・・・パケット受は部。
FIG. 1 is a detailed explanatory diagram of the present invention, FIGS. 2A and 2B are explanatory diagrams of a conventional charging method, and FIG. 3 is a diagram showing the arrangement of a coke dry extinguishing system in a coke oven. DESCRIPTION OF SYMBOLS 1... Crane, 2... Hoisting drum, 4-... Hanging beam, 5... Hanging hook, 6... Cork baguette, 7... Hanging rod, 8... Opening/closing link connection fittings, 9...Damper 10...Damper opening/closing link, 11...Packet receiver part.

Claims (1)

【特許請求の範囲】[Claims] 複数のコークス乾式消化装置一つの冷却塔に、コークバ
ッケトの赤熱コークスを装入するに際し、コークバケッ
トのダンパーを途中開度に維持して所定時間装入し、コ
ークバケット内にコークスの一部を残してダンパーを全
閉とし、残りのコークスを他の冷却塔に装入することを
特徴とするコークス乾式消火装置冷却塔への分割装入方
法。
When charging red-hot coke from a coke bucket into the cooling tower of a single coke dry digester, the damper of the coke bucket is kept partially open and the coke is charged for a predetermined period of time, leaving some of the coke inside the coke bucket. A method for charging a coke dry extinguishing system into a cooling tower in divided manner, characterized by completely closing a damper and charging the remaining coke into another cooling tower.
JP1200880A 1989-08-02 1989-08-02 Split charging method for coke dry fire extinguishing system cooling tower Pending JPH0364392A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1200880A JPH0364392A (en) 1989-08-02 1989-08-02 Split charging method for coke dry fire extinguishing system cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1200880A JPH0364392A (en) 1989-08-02 1989-08-02 Split charging method for coke dry fire extinguishing system cooling tower

Publications (1)

Publication Number Publication Date
JPH0364392A true JPH0364392A (en) 1991-03-19

Family

ID=16431777

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1200880A Pending JPH0364392A (en) 1989-08-02 1989-08-02 Split charging method for coke dry fire extinguishing system cooling tower

Country Status (1)

Country Link
JP (1) JPH0364392A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018150721A1 (en) * 2017-02-14 2018-08-23 スチールプランテック株式会社 Coke dry quenching plant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018150721A1 (en) * 2017-02-14 2018-08-23 スチールプランテック株式会社 Coke dry quenching plant
TWI665296B (en) * 2017-02-14 2019-07-11 日商製鐵設備技術股份有限公司 Coke dry quenching facility
CN110249032A (en) * 2017-02-14 2019-09-17 钢铁普蓝特克股份有限公司 Coke dry quenching facility

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