JP2000282046A - Coke dry quenching facility - Google Patents

Coke dry quenching facility

Info

Publication number
JP2000282046A
JP2000282046A JP11095506A JP9550699A JP2000282046A JP 2000282046 A JP2000282046 A JP 2000282046A JP 11095506 A JP11095506 A JP 11095506A JP 9550699 A JP9550699 A JP 9550699A JP 2000282046 A JP2000282046 A JP 2000282046A
Authority
JP
Japan
Prior art keywords
coke
cooling
chamber
cooling chamber
fire extinguishing
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.)
Withdrawn
Application number
JP11095506A
Other languages
Japanese (ja)
Inventor
Yoshinori Ishida
芳紀 石田
Kosuke Yokote
孝輔 横手
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
Nippon Steel Plant Designing Corp
Original Assignee
Nittetsu Plant Designing Corp
Nippon Steel Corp
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 Nittetsu Plant Designing Corp, Nippon Steel Corp filed Critical Nittetsu Plant Designing Corp
Priority to JP11095506A priority Critical patent/JP2000282046A/en
Publication of JP2000282046A publication Critical patent/JP2000282046A/en
Withdrawn legal-status Critical Current

Links

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  • Coke Industry (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a coke dry quenching facility in which coke body structure becomes firm and coke particle size distribution in a cooling chamber is improved. SOLUTION: In this coke dry quenching facility equipped with a cooling chamber 2 for cooling red-heat coke by blowing a cooling gas into the coke and a pre-chamber 1 installed in the upper part, the upper part of the cooling chamber 2 is made to communicate through plural coke charge pipes 6 provided at intervals in the circumferential direction of the cooling chamber 2 with the lower part of the cooling chamber 2 and a cooling gas sucking pipe 3 is provided in the center of the upper part of the cooling chamber 2.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、コークス炉から排
出される赤熱コークスを冷却するコークス乾式消火設備
に関する。
The present invention relates to a coke dry fire extinguishing system for cooling red hot coke discharged from a coke oven.

【0002】[0002]

【従来の技術】図3及び図4は従来のコークス乾式消火
設備の断面図で、図3において、コークス乾式消火設備
20は、赤熱コークスを冷却する冷却室21と、その上
部に設けられたプレチャンバー22とが煉瓦で構成さ
れ、プレチャンバー22はコークス炉から断続的に供給
される赤熱コークス量の変動緩和の役割をする。冷却室
21とプレチャンバー22との間に熱交換された高温ガ
スを抜き出す複数のスローピングフリュー23が環状に
設けられ、スローピングフリュー23に連通する環状ダ
クト24がプレチャンバー22の内筒煉瓦壁の外周部に
形成され、環状ダクト24の排ガスは除塵器を経てボイ
ラに導入される。
2. Description of the Related Art FIGS. 3 and 4 are cross-sectional views of a conventional coke dry fire extinguishing system. In FIG. 3, a coke dry fire extinguishing system 20 includes a cooling chamber 21 for cooling red hot coke and a pre-cooling chamber provided at an upper portion thereof. The chamber 22 is made of a brick, and the pre-chamber 22 plays a role in reducing the fluctuation of the amount of red hot coke intermittently supplied from the coke oven. A plurality of sloping flues 23 for extracting the high-temperature gas exchanged between the cooling chamber 21 and the pre-chamber 22 are provided in an annular shape, and an annular duct 24 communicating with the sloping flu 23 is formed around the inner cylindrical brick wall of the pre-chamber 22. The exhaust gas from the annular duct 24 is introduced into the boiler via a dust remover.

【0003】また、図4に示すように、実公昭58−4
909号公報には、円筒状のバンカ本体31の天床の中
央部に熱ガス出口32が設けられ、周辺部に複数の赤熱
コークス供給口33が設けられている。赤熱コークス供
給口33は、1個のコークス投入口34から分岐された
4本の分岐路35の下端開口によって構成され、バンカ
本体31の下部中央には冷却気体分配器36が設けら
れ、冷却気体を放出する。バンカ本体31の下端にはコ
ークス取出口37が設けられている。
Further, as shown in FIG.
In Japanese Patent Application Laid-Open No. 909, a hot gas outlet 32 is provided at the center of the top floor of a cylindrical bunker main body 31, and a plurality of red hot coke supply ports 33 are provided at a peripheral portion. The red hot coke supply port 33 is constituted by the lower end openings of four branch passages 35 branched from one coke input port 34, and a cooling gas distributor 36 is provided in the lower center of the bunker body 31, and the cooling gas distributor 36 is provided. Release. A coke outlet 37 is provided at the lower end of the bunker body 31.

【0004】[0004]

【発明が解決しようとする課題】図3に示すコークス乾
式消火設備では、スローピングフリュー部は煉瓦構造の
ため、強度的に弱いので、設備を大型化する場合、コー
クス冷却ガス通過面積を増加することが困難である。ま
た、操業年数が多くなると、補修の必要があり、その費
用と設備停止期間が多く掛かるという欠点がある。ま
た、コークスを中央から投入するので、中央が高い山形
状となり、大塊コークスが周辺に集まり、逆に中央部に
細かいコークスが集まるため、冷却ガスは周辺に多く、
中央部はほとんど流れない傾向があり冷却効率が低かっ
た。
In the coke dry fire extinguishing system shown in FIG. 3, since the sloping flue portion is of a brick structure and thus weak in strength, the coke cooling gas passage area must be increased when enlarging the facility. Is difficult. In addition, as the number of years of operation increases, it is necessary to perform repairs, and there is a drawback that costs and equipment downtime are increased. Also, since coke is injected from the center, the center becomes a high mountain shape, large lump coke gathers around, and conversely, fine coke gathers in the center, so there is a lot of cooling gas around,
The central part tended to hardly flow and the cooling efficiency was low.

【0005】また、図4に示すコークス乾式消火設備で
は、コークス炉からのコークス供給は、バッチ方式であ
り、常時、コークス堆積表面位置が上下し、バンカ内の
コークス量が変動するため、熱ガス出口32のガス温度
も変動し、ボイラ入口のガス温度も変動し、安定した操
業が困難となる。また、上部入口を開にした場合、その
下部の分岐路が空間になっており、熱ガス出口までに抵
抗となるものが何もないので、容易に多量の空気を吸入
して、この空気がコークス表面で燃焼し、熱ガス出口の
温度を変動させるという欠点がある。
Further, in the coke dry-type fire extinguishing system shown in FIG. 4, coke is supplied from a coke oven in a batch system, and the coke deposition surface position always fluctuates and the amount of coke in the bunker fluctuates. The gas temperature at the outlet 32 also fluctuates, and the gas temperature at the boiler inlet fluctuates, making stable operation difficult. Also, when the upper inlet is opened, the lower branch is a space, and there is nothing that becomes a resistance to the hot gas outlet. There is a disadvantage in that it burns on the coke surface and fluctuates the temperature of the hot gas outlet.

【0006】本発明は、炉体構造が強固になり、また、
冷却室内のコークス粒度分布が改善されるコークス乾式
消火設備を提供するものである。
According to the present invention, the furnace body structure is strengthened,
An object of the present invention is to provide a coke dry fire extinguishing system in which the coke particle size distribution in a cooling chamber is improved.

【0007】[0007]

【課題を解決するための手段】本発明のコークス乾式消
火設備は、冷却ガスを吹き込んで赤熱コークスを冷却す
る冷却室とその上部にプレチャンバーが設置されたコー
クス乾式消火設備であって、冷却室の上部とプレチャン
バーの下部とが、冷却室の円周方向に間隔をおいて設け
られた複数のコークス投入管を介して連通しており、冷
却室の上部の中央には冷却ガス吸引管を設けたことを特
徴とする。
A coke dry-fire extinguishing system according to the present invention is a coke dry-type fire extinguishing system in which a cooling gas is blown to cool red-hot coke and a pre-chamber is provided above the cooling room. And the lower part of the pre-chamber communicate with each other through a plurality of coke charging pipes provided at intervals in the circumferential direction of the cooling chamber, and a cooling gas suction pipe is provided at the center of the upper part of the cooling chamber. It is characterized by having been provided.

【0008】[0008]

【発明の実施の形態】図1は本発明のコークス乾式消火
設備の縦断面図、図2は同斜視図である。コークス乾式
消火設備は、上部のプレチャンバー1とその下部に連設
された冷却室2とから構成される。冷却室2の天井の中
央には、冷却ガスを吸引する冷却ガス吸引管3が設けら
れ、冷却室2の底部には冷却ガスを吹き込む冷却ガス供
給管(図示せず)及びコークス排出口4が設けられてい
る。
FIG. 1 is a longitudinal sectional view of a coke dry fire extinguishing system of the present invention, and FIG. 2 is a perspective view of the same. The coke dry fire extinguishing system is composed of an upper pre-chamber 1 and a cooling chamber 2 connected to a lower part thereof. A cooling gas suction pipe 3 for sucking a cooling gas is provided at the center of the ceiling of the cooling chamber 2, and a cooling gas supply pipe (not shown) for blowing the cooling gas and a coke outlet 4 are provided at the bottom of the cooling chamber 2. Is provided.

【0009】プレチャンバー1の上部には赤熱コークス
投入口5が設けられ、下部には複数のコークス投入管6
が冷却室2の円周方向に間隔をおいて設けられ、コーク
ス投入管6の下端は冷却室2の天井に接続し、プレチャ
ンバー1と冷却室2とはコークス投入管6を介して連通
する。
A red hot coke input port 5 is provided at the upper part of the pre-chamber 1 and a plurality of coke input pipes 6 are provided at the lower part.
Are provided at intervals in the circumferential direction of the cooling chamber 2, the lower end of the coke charging pipe 6 is connected to the ceiling of the cooling chamber 2, and the pre-chamber 1 and the cooling chamber 2 communicate with each other via the coke charging pipe 6. .

【0010】前記構成において、プレチャンバー1上部
に設置されたホッパーから赤熱コークスを赤熱コークス
投入口5からプレチャンバー1に投入する。投入された
コークスは、プレチャンバー1からコークス投入管6を
下降し、冷却室2へ装入され、コークスは冷却ガスと熱
交換され、冷却されて冷却室2のコークス排出口4から
排出される。熟交換して暖められたガスは中央部の冷却
ガス吸引管3で吸引されボイラ側へ供給される。
In the above configuration, red hot coke is injected into the pre-chamber 1 from the red hot coke input port 5 from a hopper installed above the pre-chamber 1. The injected coke descends from the pre-chamber 1 through the coke input pipe 6 and is charged into the cooling chamber 2, where the coke is exchanged with the cooling gas and cooled, and is discharged from the coke outlet 4 of the cooling chamber 2. . The gas warmed by the ripening exchange is sucked by the cooling gas suction pipe 3 at the center and supplied to the boiler side.

【0011】本発明においては、コークス投入管内にコ
ークスを貯留することにより、冷却室内では冷却ガスと
熱交換を行うコークス量は一定となり、冷却ガス吸引管
入口でのガス温度を一定に保つことができる。また、コ
ークス投入管内にコークスを貯留するので、上部のコー
クス投入口を開にしても多量の空気を吸引することがな
いので、熱ガス温度が一定となり、安定操業が可能とな
る。
In the present invention, by storing coke in the coke charging pipe, the amount of coke that exchanges heat with the cooling gas in the cooling chamber becomes constant, and the gas temperature at the inlet of the cooling gas suction pipe can be kept constant. it can. Further, since coke is stored in the coke charging pipe, a large amount of air is not sucked even when the upper coke charging port is opened, so that the hot gas temperature becomes constant and stable operation becomes possible.

【0012】[0012]

【発明の効果】本発明は、従来の弱体な煉瓦構造である
スローピングフリューをなくすことによって、構造の安
定化を図ることができる。また、コークス投入管により
コークスを周辺から投入するので、冷却ガスの流れにく
い中央部に大塊コークスが集まり易く、冷却塔内の熱交
換効率も従来方法に比べて改善される。
According to the present invention, the structure can be stabilized by eliminating the sloping flue which is a conventional weak brick structure. Further, since coke is introduced from the periphery by the coke introduction pipe, large coke is easily collected in the central portion where the flow of the cooling gas is difficult, and the heat exchange efficiency in the cooling tower is improved as compared with the conventional method.

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

【図1】 本発明のコークス乾式消火設備の縦断面図で
ある。
FIG. 1 is a longitudinal sectional view of a coke dry fire extinguishing facility of the present invention.

【図2】 本発明のコークス乾式消火設備の斜視図であ
る。
FIG. 2 is a perspective view of a coke dry fire extinguishing facility of the present invention.

【図3】 従来のコークス乾式消火設備の断面図であ
る。
FIG. 3 is a cross-sectional view of a conventional coke dry fire extinguishing system.

【図4】 従来の別のコークス乾式消火設備の断面図で
ある。
FIG. 4 is a sectional view of another conventional coke dry fire extinguishing system.

【符号の説明】[Explanation of symbols]

1:プレチャンバー 2:冷却室 3:冷却ガ
ス吸引管 4:コークス排出口 5:赤熱コークス投入口
6:コークス投入管 20:コークス乾式消火設備 21:冷却室
22:プレチャンバー 23:スローピングフリュー 24:環状ダクト
31:バンカ本体 32:熱ガス出口 33:赤熱コークス供給口 34:コークス投入口 35:分岐路 36:
冷却気体分配器 37:コークス取出口
1: Prechamber 2: Cooling chamber 3: Cooling gas suction pipe 4: Coke outlet 5: Red hot coke inlet
6: Coke input pipe 20: Coke dry fire extinguishing equipment 21: Cooling room
22: Pre-chamber 23: Sloping flue 24: Annular duct
31: Bunker main body 32: Hot gas outlet 33: Red hot coke supply port 34: Coke input port 35: Branch path 36:
Cooling gas distributor 37: Coke outlet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 横手 孝輔 北九州市戸畑区大字中原46−59 新日本製 鐵株式会社エンジニアリング事業本部内 Fターム(参考) 4H012 DA02  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Kosuke Yokote 46-59, Nakahara, Tobata-ku, Kitakyushu F-term in the Nippon Steel Corporation Engineering Division (Reference) 4H012 DA02

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 冷却ガスを吹き込んで赤熱コークスを冷
却する冷却室とその上部にプレチャンバーが設置された
コークス乾式消火設備であって、冷却室の上部とプレチ
ャンバーの下部とが、冷却室の円周方向に間隔をおいて
設けられた複数のコークス投入管を介して連通してお
り、冷却室の上部の中央には冷却ガス吸引管を設けたこ
とを特徴とするコークス乾式消火設備。
1. A coke dry fire extinguishing system in which a cooling gas is blown to cool red hot coke and a pre-chamber is installed above the cooling chamber, wherein an upper part of the cooling chamber and a lower part of the pre-chamber are connected to each other by a cooling chamber. A coke dry fire extinguishing system characterized in that it communicates via a plurality of coke inlet pipes provided at intervals in the circumferential direction, and a cooling gas suction pipe is provided at the center of the upper part of the cooling chamber.
JP11095506A 1999-04-01 1999-04-01 Coke dry quenching facility Withdrawn JP2000282046A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11095506A JP2000282046A (en) 1999-04-01 1999-04-01 Coke dry quenching facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11095506A JP2000282046A (en) 1999-04-01 1999-04-01 Coke dry quenching facility

Publications (1)

Publication Number Publication Date
JP2000282046A true JP2000282046A (en) 2000-10-10

Family

ID=14139490

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11095506A Withdrawn JP2000282046A (en) 1999-04-01 1999-04-01 Coke dry quenching facility

Country Status (1)

Country Link
JP (1) JP2000282046A (en)

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Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20060606