JPS61197685A - Removal of carbon deposits in carbonization chamber and riser of coke oven - Google Patents

Removal of carbon deposits in carbonization chamber and riser of coke oven

Info

Publication number
JPS61197685A
JPS61197685A JP3757885A JP3757885A JPS61197685A JP S61197685 A JPS61197685 A JP S61197685A JP 3757885 A JP3757885 A JP 3757885A JP 3757885 A JP3757885 A JP 3757885A JP S61197685 A JPS61197685 A JP S61197685A
Authority
JP
Japan
Prior art keywords
carbon
gas
coke oven
riser
coke
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
JP3757885A
Other languages
Japanese (ja)
Inventor
Yoshihiko Morishita
森下 良彦
Shigeru Ohashi
大橋 茂
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 JP3757885A priority Critical patent/JPS61197685A/en
Publication of JPS61197685A publication Critical patent/JPS61197685A/en
Pending legal-status Critical Current

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  • Industrial Gases (AREA)

Abstract

PURPOSE:To remove deposited carbon in a short time and utilize recovered gas effectively, by blowing a gas which contains a large amount of CO2 into a carbonizing chamber of a coke oven to gasify carbon deposited in the carbonizing chamber and the riser. CONSTITUTION:In dry distillation of coal, a gas which contains a large amount of CO2 (e.g. coke oven waste gas or blast furnace gas) is blown into a carboniz ing chamber 1 of a coke oven through blowing burners 2a, 2b and 2c so that carbon 5 deposited in the carbonizing chamber 1 and the upstanding part of a riser 6 may react with CO2 for gasification according to the reaction formula. The gasified carbon is suctioned by ejection with an ammonia water spray 9 and recovered into a dry main 8 via the riser 6. The method makes it possible to remove carbon deposits in a short time and improve the productivity of coke.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、コークス炉炭化室及び上昇管に付着するカー
ボンの除去方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for removing carbon adhering to a coke oven carbonization chamber and riser pipe.

〔従来の技術〕[Conventional technology]

コークス製造用コークス炉の炭化室および炭化ガス引抜
き用の上昇管には098〜99%残部Aih分よシなる
カーボンがそれらの内壁に付着する。
Carbon with a balance of 098 to 99% Aih adheres to the inner walls of the coking chamber and riser pipe for drawing out carbonized gas in a coke oven for producing coke.

これらカーボンを放置すると装炭ならびに押出し九当っ
て支障となるので除去する必要がある。
If these carbons are left unattended, they will interfere with carburization and extrusion, so they must be removed.

従って上記カーボンの除去に当っては、カーボンが高温
雰囲気でかつ固着しているため専らカーボンの燃焼忙よ
る除去が行なわれてきた。燃焼による付着カーボン除去
方法は空窯の際に上昇管蓋7を開放し、次いで装入口の
蓋を開放し、ドラフト効果により空気を吸引し、カーボ
ンを燃焼させ大気中に放出していた。然しなから従来付
着カーボンの状態例えばその厚み、大きさによって除去
時間が長くなるもの、また一度に燃焼処理できないこと
がある。そうした場合、一般にコークス炉作業は、コー
クスを押し出した直後に、石炭の装入を行なうことを基
調とするものであるが、付着カーボンの燃焼除去は、コ
ークスの押し出しの後、石炭を装入せずに所謂9窯の状
態で行なわれ、その除去時間は短いものでも2時間長い
ものは20時間程度も要する。
Therefore, in removing the above-mentioned carbon, since the carbon is fixed in a high-temperature atmosphere, removal has been carried out exclusively by combustion of the carbon. The method for removing attached carbon by combustion involves opening the riser pipe cover 7 when the kiln is empty, then opening the charge port cover, sucking air by a draft effect, burning the carbon, and releasing it into the atmosphere. However, conventionally, depending on the condition of the deposited carbon, such as its thickness and size, it may take a long time to remove it, or it may not be possible to burn it all at once. In such cases, coke oven operations are generally based on charging coal immediately after extruding coke, but in order to burn off the adhering carbon, it is necessary to charge coal immediately after extruding coke. The removal time is carried out in so-called 9 kilns, and the removal time is as long as 2 hours for the shortest one, and about 20 hours for the longest one.

従ってコークスの生産活動に影響を与えるばかりでなく
、殆ど煉瓦よシなるコークス炉そのものの劣化をも進行
せしめる。
Therefore, it not only affects coke production activities, but also accelerates the deterioration of the coke oven itself, which is mostly made of bricks.

この几め付着カーボンをコークス炉の損傷なくかつ生産
活動に影響を与えることなく除去し、かつ付着カニボン
の有効利用を図る方法の開発が待望されていた。
There has been a long-awaited development of a method to remove this thickened carbon without damaging the coke oven or affecting production activities, and to effectively utilize the carbon stuck to the coke oven.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明は、コークス炉炭化室及び上昇管等罠付着するカ
ーボンを、短時間に除去し、かつ付着カーボンをガス化
し回収しその回収ガスを有効に活用できる付着カーボン
の除去方法を提供することを目的とする。
The present invention aims to provide a method for removing adhering carbon that can remove adhering carbon in traps such as coke oven carbonization chambers and riser pipes in a short time, gasify and recover the adhering carbon, and effectively utilize the recovered gas. purpose.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は、付着カーボンそのものがカーボンであるこ
とに着目し、前述の問題点及び要望に答えるべく本発明
に至ったものである。
The present inventor has focused on the fact that the deposited carbon itself is carbon, and has arrived at the present invention in order to solve the above-mentioned problems and demands.

即ち本発明は、石炭乾留中、乾留末期、及び乾留後にお
いて、炭化室内に、C02を多量に含むガスを吹込み、
付着カーボンとCO,ガスとを反応せしめガス化し、そ
の反応ガスを従来のコークス炉ガスと一緒にドライメン
(集気管)に回収し所定のガス処理工程を経て有効利用
するものである。
That is, the present invention injects a gas containing a large amount of CO2 into the carbonization chamber during coal carbonization, at the final stage of carbonization, and after carbonization,
The deposited carbon is reacted with CO and gas to be gasified, and the reaction gas is collected together with conventional coke oven gas into a dry men (air collecting pipe) and effectively utilized through a predetermined gas treatment process.

〔作 用〕[For production]

本発明方法においてCot t”多量に含むガスを炭化
室内に吹込むものであるが、このガスと付着カーボンと
の間において、 Co!+ C= 2CO・・・・・・(1)の反応を起
さしめ付着カーボンをガス化せしめるものである。この
(1)式の反応は吸熱反応である次め炉を冷やす懸念が
ある。
In the method of the present invention, a gas containing a large amount of "Cot t" is blown into the carbonization chamber, and the reaction of Co!+ C= 2CO (1) occurs between this gas and the deposited carbon. The reaction of formula (1) is an endothermic reaction and there is a concern that it may cool the furnace.

従って、(1)式の反応を進めるために一部熱を供給す
る必要があるが、コークス炉内は可燃ガス(COガス)
、カーボンが存在しまた燃焼温度に十分達しているので
、若干のOS分を供給するだけで熱供給は可能である。
Therefore, it is necessary to supply some heat to advance the reaction in equation (1), but the inside of the coke oven is filled with flammable gas (CO gas).
Since carbon is present and the combustion temperature has been sufficiently reached, heat can be supplied by simply supplying a small amount of OS.

但しOSだけの供給は供給部の局部的燃焼を発生せしめ
、コークス炉煉瓦及び金物の劣化を誘発する懸念がある
ため、燃焼速度をコントロールしながら即ちCO,とO
雪の比率を00220〜100% 020〜10%の範
凹に適度に制御し炭化室内のカーボンをガス化させ、更
にそのガスを回収するものである。
However, since there is a concern that supplying only OS may cause local combustion in the supply section and induce deterioration of coke oven bricks and hardware, it is necessary to control the combustion rate while controlling the combustion rate.
The snow ratio is appropriately controlled within the range of 0.220% to 100% to 0.20% to 10%, the carbon in the carbonization chamber is gasified, and the gas is recovered.

〔実施例〕〔Example〕

次に本発明を、カールスチル型コークス炉の炭化室及び
上昇管に適用し次側について述べる。
Next, the present invention will be applied to the carbonization chamber and riser pipe of a Karlstil type coke oven, and the subsequent aspects will be described.

第1図及び第2図は、上記炉の炭化室及び上昇管の夫々
コークス充填時及び空窯時の本発明方法の説明図である
FIGS. 1 and 2 are explanatory diagrams of the method of the present invention when the carbonization chamber and riser pipe of the above-mentioned furnace are filled with coke and when the oven is empty, respectively.

第1図及び第2図において1はコークス炉炭化室で炉幅
450箇、炉高7550■(有効7200■)炉長17
000鴫(有効16200■)有効内容積52.5rr
!の仕様のものである。コークス押し出した後の空窯時
の場合第2図に示す如くガス吹込みバーナ2を石炭装入
口(400■φ)3ならびにコークス炉炉蓋4を貫通し
て設け、Co、を多量に含むガス例えばコークス炉廃ガ
ス、高炉ガス(Bガス)、その他CO鵞を多量に含むガ
スをガス吹込みバーナ2m、2b、2cより炭化室1内
に吹込み、前記(1)式の反応によシ、炭化室内の煉瓦
表面並に上昇管立上り部に付着したカーボン(C:98
〜99 S  Ash  1〜2 % ) 5 tカス
化L、又一方コークス充てん時の場合は第1図に示す如
くしてガス化し、安水スプレー9によるエジェクション
によシ吸引し上昇管6を経由してドライメン8に通常の
乾留ガスと一緒に回収する。
In Figures 1 and 2, 1 is a coke oven carbonization chamber with a width of 450 mm, a height of 7550 mm (effective 7200 mm), and a length of 17 mm.
000 Tsuku (effective 16200■) Effective internal volume 52.5rr
! The specifications are as follows. In the case of an empty oven after extruding coke, a gas injection burner 2 is installed through the coal charging port (400 mm) 3 and the coke oven cover 4 as shown in Fig. 2, and a gas injection burner containing a large amount of Co is installed. For example, coke oven waste gas, blast furnace gas (B gas), and other gases containing a large amount of CO are blown into the carbonization chamber 1 from the gas injection burners 2m, 2b, and 2c, and the reaction of equation (1) is performed. , Carbon (C: 98
~99 S Ash 1~2%) 5 t into scum L, or on the other hand, in the case of coke filling, it is gasified as shown in FIG. The gas is collected via Drymen 8 together with normal carbonization gas.

石炭装入量1a3t/窯サイクル、稼動率130チの操
業条件で生成される付着カーボン5の量は1〜10に9
/室乾留サイクルで、コークス充填時は第1図に示す如
く吹込みバーナ2aより Co、を多量に含む燃焼廃ガ
ス例えばガス組成(容量%)Co、:30%O! : 
5%Nt : 65%’に2時間吹込ミカス化しCO6
度23%の回収ガスを通常乾留ガスと一緒にドライメン
8にて回収し、空窯時は第2図に示す如く吹込みバーナ
2b、2cよシ上記燃焼廃ガスを、窯出し槃備時間の約
1〜1.5時間内に吹込み、回収し別に設けた配管によ
り有効に利用するO 以上のようなガス吹込作業を2〜10乾留サイクル平均
5乾留サイクル毎に実施した結果付着カーボンは除去さ
れ、操業の稼動率は1〜2%向上し念。
The amount of adhered carbon 5 produced under the operating conditions of 1a3t coal charge/kiln cycle and 130cm operating rate is 1 to 10 times 9.
/ chamber carbonization cycle, when charging coke, as shown in Fig. 1, combustion waste gas containing a large amount of Co is emitted from the blowing burner 2a as shown in Fig. 1. For example, gas composition (volume %) Co: 30% O! :
5%Nt: Blow to 65% for 2 hours to make CO6
The recovered gas with a concentration of 23% is collected together with the normal carbonization gas in the dry men 8, and when the kiln is empty, the combustion waste gas is transferred to the blow burners 2b and 2c as shown in Fig. 2. O is injected within about 1 to 1.5 hours, collected, and effectively used by separate piping.As a result of performing the above gas blowing work every 2 to 10 carbonization cycles, on average every 5 carbonization cycles, the attached carbon is removed. It is expected that the operating rate will improve by 1-2%.

なおCO,を多量に含むガス吹込みにおいて、炭化室内
温度はコークス充填時は900〜850℃合0!含有量
の多い燃焼廃ガスを吹込みC02とO。
In addition, when blowing gas containing a large amount of CO, the temperature inside the carbonization chamber is 900 to 850 degrees Celsius when coke is filled. Blow in combustion waste gas with a high content of CO2 and O.

との成分比率を調整した。The component ratio was adjusted.

〔発明の効果〕〔Effect of the invention〕

本発明の付着カーボン除去方法は、短時間に付着カーボ
ンを除去し得るため、コークスの生産性を従来よシ向上
せしめるものであシ、かつガス化せしめるのでその回収
ガスは有効に回収利用しうる効果を奏するものである。
The method for removing adhering carbon of the present invention can remove adhering carbon in a short time, thereby improving coke productivity compared to the conventional method, and since it is gasified, the recovered gas can be effectively recovered and used. It is effective.

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

第1図及び第2図は夫々コークス充填時及び空窯時の本
発明方法の説明図である。 図において1:炭化室、2:吹込みバーナ、3:石炭装
入口、4:炉蓋、5:付着カーボン、6:上昇管、7:
上部蓋、8ニドライメン、9:安水スプレィ。 なお各図中、同一符号は同−又は相当部分を示すO 代理人 弁理士  木 村 三 朗 −〜
FIGS. 1 and 2 are explanatory diagrams of the method of the present invention during coke filling and an empty oven, respectively. In the figure, 1: carbonization chamber, 2: blowing burner, 3: coal charging port, 4: furnace lid, 5: deposited carbon, 6: riser pipe, 7:
Top lid, 8 Ni Dry Men, 9: Anhydrous spray. In each figure, the same reference numerals indicate the same or corresponding parts.O Agent: Patent Attorney Sanro Kimura

Claims (1)

【特許請求の範囲】[Claims] コークス炉内の付着カーボンを除去するためにCO_2
を多量に含有するガスを炭化室内に吹込み、該付着カー
ボンをガス化させることを特徴とするコークス炉炭化室
及び上昇管の付着カーボンの除去方法。
CO_2 to remove adhering carbon in the coke oven
A method for removing deposited carbon from a coke oven carbonization chamber and a riser pipe, comprising blowing gas containing a large amount of carbon into the carbonization chamber to gasify the deposited carbon.
JP3757885A 1985-02-28 1985-02-28 Removal of carbon deposits in carbonization chamber and riser of coke oven Pending JPS61197685A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3757885A JPS61197685A (en) 1985-02-28 1985-02-28 Removal of carbon deposits in carbonization chamber and riser of coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3757885A JPS61197685A (en) 1985-02-28 1985-02-28 Removal of carbon deposits in carbonization chamber and riser of coke oven

Publications (1)

Publication Number Publication Date
JPS61197685A true JPS61197685A (en) 1986-09-01

Family

ID=12501418

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3757885A Pending JPS61197685A (en) 1985-02-28 1985-02-28 Removal of carbon deposits in carbonization chamber and riser of coke oven

Country Status (1)

Country Link
JP (1) JPS61197685A (en)

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