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JPH0776371B2 - Blast furnace operation method - Google Patents
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JPH0776371B2 - Blast furnace operation method - Google Patents

Blast furnace operation method

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Publication number
JPH0776371B2
JPH0776371B2 JP61262697A JP26269786A JPH0776371B2 JP H0776371 B2 JPH0776371 B2 JP H0776371B2 JP 61262697 A JP61262697 A JP 61262697A JP 26269786 A JP26269786 A JP 26269786A JP H0776371 B2 JPH0776371 B2 JP H0776371B2
Authority
JP
Japan
Prior art keywords
air
water
branch pipe
furnace
tuyere
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 - Lifetime
Application number
JP61262697A
Other languages
Japanese (ja)
Other versions
JPS63118006A (en
Inventor
道浩 船木
均 吉田
裕二 佐藤
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
Original Assignee
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP61262697A priority Critical patent/JPH0776371B2/en
Publication of JPS63118006A publication Critical patent/JPS63118006A/en
Publication of JPH0776371B2 publication Critical patent/JPH0776371B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、羽口に接続された送風支管毎に支管風量計、
水又は水蒸気吹き込みノズルを設け、上記ノズル毎に水
又は水蒸気吹き込み量を制御する水又は水蒸気吹き込み
量制御弁を設けた高炉の操業方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of use) The present invention relates to a branch pipe air flow meter for each blower branch pipe connected to a tuyere,
The present invention relates to a method for operating a blast furnace in which a water or steam blowing nozzle is provided and a water or steam blowing amount control valve for controlling the amount of water or steam blowing is provided for each nozzle.

(従来の技術) 高炉操業を安定させるためには、高炉の円周方向の炉内
ガス分布を均一にする必要がある。そのためには炉内円
周方向の通気性を均一にすると共に各羽口からの送風量
を均一にする必要がある。
(Prior Art) In order to stabilize the operation of the blast furnace, it is necessary to make the gas distribution in the furnace in the circumferential direction of the blast furnace uniform. For that purpose, it is necessary to make the air permeability in the circumferential direction of the furnace uniform and the air flow from each tuyere uniform.

ところが一般に高炉の炉内への送風は、送風機より冷風
を熱風炉へ送り、送風機より熱風炉への冷風管内への水
蒸気添加又は散水で調湿された冷風を熱風炉で1000〜12
00℃の熱風となし熱風管、環状管を通って、各送風支管
を介して各羽口より行う。
However, in general, for blowing air into the furnace of a blast furnace, cold air is sent from a blower to a hot air stove, and cold air that has been conditioned by adding steam or sprinkling water to the hot air stove from the air blower to a hot air stove 1000 to 12
It is done from each tuyere through each blast branch pipe through the hot air pipe of 00 ℃ and the hot air pipe and ring pipe.

なお上記送風湿分の調整を送風支管毎に水又は水蒸気吹
き込みノズルを設け、上記ノズル毎に水又は水蒸気吹き
込み量を制御する水又は水蒸気吹き込み量制御弁を設け
て、羽口毎に独立して調湿送風できるようにしたものも
特開昭58−87210号、特開昭58−87211号公報等で知られ
ている。
It should be noted that the adjustment of the blast moisture content is provided with a water or steam blowing nozzle for each blast branch pipe, and a water or steam blowing amount control valve for controlling the amount of water or steam blowing is provided for each nozzle, independently for each tuyere. Those capable of controlling humidity are also known in JP-A-58-87210 and JP-A-58-87211.

上記の如く高炉送風設備は、環状管と熱風炉が通常単一
の熱風管により接続されているため、炉内円周方向の通
気性が均一であっても、熱風管の接続部に近い羽口と遠
い羽口とでは炉内への送風量が異なってくる。
As described above, in the blast furnace ventilation equipment, the annular pipe and the hot air stove are usually connected by a single hot air pipe, so even if the air permeability in the circumferential direction in the furnace is uniform, the blades close to the hot air pipe connection part The amount of air blown into the furnace differs between the mouth and the distant tuyere.

このような高炉送風設備上の各羽口からの送風量の不均
一は、各羽口の口径の変更、送風支管に設けた支管風量
制御弁の弁開度の設定変更(特公昭53−13325号公報、
特開昭60−114511号公報)によって解消できる。また高
炉の環状管を複数に分割し、各分割した環状管にそれぞ
れ熱風管、熱風炉、送風機を接続し、各環状管毎に独立
した送風系を設置(特公昭48−39122号公報)したり、
送風支管群を高炉周方向に沿って複数の送風支管群に分
割し、この送風支管群を各送風支管群毎に設けた分配管
に接続し、各分配管を連通管を介して環状管に接続し、
各連通管に流量調節弁を設置する(特公昭57−52923号
公報)ことによっても解消できる。
Such non-uniformity of the air flow from each tuyere on the blast furnace blast equipment is caused by changing the diameter of each tuyere and the setting of the valve opening of the branch air flow control valve provided on the blast branch pipe (Japanese Patent Publication No. 53-13325). Bulletin,
The problem can be solved by JP-A-60-114511. In addition, the annular tube of the blast furnace was divided into multiple parts, and each of the divided annular tubes was connected with a hot air tube, a hot air oven, and a blower, and an independent air blowing system was installed for each annular tube (Japanese Patent Publication No. 48-39122). Or
The blast branch pipe group is divided into multiple blast branch pipe groups along the circumferential direction of the blast furnace, this blast branch pipe group is connected to the distribution pipes provided for each blast branch pipe group, and each distribution pipe is connected to an annular pipe through a communication pipe. connection,
It can also be solved by installing a flow rate control valve in each communication pipe (Japanese Patent Publication No. 57-52923).

尚、炉内円周方向の通気性が均一であれば、上記のよう
に各羽口からの送風量が均一となるように構成され、且
つ特開昭50−68908号公報に提案される如く送風支管毎
に支管風量計を設けた高炉においては、上記各支管風量
計で測定される各支管風量は各羽口前の炉内通気性を示
し、上記支管風量計群で測定される支管風量群は炉内円
周方向の通気性を示す。
As long as the air permeability in the circumferential direction of the furnace is uniform, the amount of air blown from each tuyere is uniform as described above, and as proposed in JP-A-50-68908. In a blast furnace equipped with a branch airflow meter for each blast branch pipe, each branch airflow measured by each branch airflow meter indicates the air permeability in the furnace before each tuyere, and the branch pipe airflow measured by the above branch airflow meter group. The group shows air permeability in the circumferential direction in the furnace.

一方、炉内円周方向の通気性の不均一は、コークス、鉱
石類の粒度偏析、原燃料性状の不均一、炉体損傷による
プロフィールの悪化等が要因となって生じる。
On the other hand, the non-uniformity of air permeability in the circumferential direction of the furnace is caused by coke, ore particle size segregation, non-uniformity of raw fuel properties, deterioration of profile due to damage to the furnace body, and the like.

(発明が解決しようとする問題点) ところでこのような炉内円周方向の通気性の不均一は、
炉頂からの装入物分布制御によって解消できるが、装入
物分布のアクションを取ったあと、その効果の見極めに
は数日必要である。即ち装入物分布制御では、炉内円周
方向の通気性の不均一を即効的には解消できない。
(Problems to be solved by the invention) By the way, such non-uniformity of air permeability in the circumferential direction of the furnace is
It can be solved by controlling the distribution of the charge from the top of the furnace, but it takes several days to determine the effect after taking the action of the distribution of the charge. That is, the charge distribution control cannot immediately eliminate the non-uniformity of air permeability in the circumferential direction of the furnace.

本発明は、羽口に接続された送風支管毎に支管風量計、
水又は水蒸気吹き込みノズルを設け、上記ノズル毎に水
又は水蒸気吹き込み量を制御する水又は水蒸気吹き込み
量制御弁を設けた高炉における新知見である上記特定羽
口の送風湿分の増加による特定羽口前の炉内通気性の即
効的改善特性を活用して、炉内円周方向の通気性の不均
一を即効的に均一にして高炉操業を安定維持することが
できる高炉操業方法を提供するものである。
The present invention is a branch air flow meter for each blow branch pipe connected to the tuyere,
A specific tuyere due to an increase in the blast moisture of the specific tuyere, which is a new finding in a blast furnace that is provided with a water or water vapor injection nozzle and a water or water vapor injection amount control valve that controls the amount of water or water vapor injection for each nozzle. (EN) A blast furnace operating method capable of rapidly maintaining uniform blast furnace operation by utilizing the immediately-improving characteristics of in-furnace air permeability to promptly make uneven the air permeability in the furnace circumferential direction. Is.

(問題点を解決するための手段) 本発明の要旨は次の通りである。(Means for Solving Problems) The gist of the present invention is as follows.

羽口に接続された送風支管毎に支管風量計、水又は水蒸
気吹き込みノズルを設け、上記ノズル毎に水又は水蒸気
吹き込み量を制御する水又は水蒸気吹き込み量制御弁を
設けた高炉において、上記支管風量計群の風量を定期的
に検出し、各送風支管均一な設定風量より風量が減少し
た送風支管の水又は水蒸気吹き込み量制御弁の開度を、
各水又は水蒸気吹き込み量制御弁均一な設定開度より増
加して水又は水蒸気を上記ノズル、送風支管、羽口を介
して炉内へ吹き込み、上記設定風量より風量が減少した
送風支管に接続された羽口前の炉内通気性を改善し、上
記水又は水蒸気吹き込み量制御弁の開度を上記設定開度
に戻すことを特徴とする高炉操業方法。
In a blast furnace equipped with a branch pipe airflow meter, a water or steam blowing nozzle for each blower branch pipe connected to the tuyere, and a water or steam blowing amount control valve for controlling the water or steam blowing amount for each nozzle, the branch pipe air amount The air volume of the meter group is regularly detected, and the opening of the air or steam injection amount control valve of the air blow branch pipe where the air volume has decreased from the uniform set air volume of each air blow branch pipe,
Each water or steam blowing amount control valve is blown into the furnace through the nozzle, blast branch pipe, and tuyere by increasing the water flow from a uniform set opening, and is connected to the blast branch pipe whose air volume is less than the set air volume. A method for operating a blast furnace, characterized in that the air permeability in the furnace before the tuyere is improved and the opening of the water or steam injection control valve is returned to the set opening.

本発明者等は、前記冷風管で散水調湿を行うと共に環状
管に単一の熱風管が接続され、第1図図示のように炉周
方向に等間隔で設けられた27本の羽口1と接続する27本
の送風支管2毎に、支管風量計3、水蒸気吹き込みノズ
ル4を設け、上記ノズル4毎に第2図の弁開度〜流量特
性を有する水蒸気吹き込み量制御弁5を設け、各羽口1
前の炉内通気性が均一であれば、各水蒸気吹き込み量制
御弁5の均一な開度、即ち全閉(開度0%)で水蒸気吹
き込みしない状態で、各羽口1からの送風量が均一とな
るように各羽口1の口径を調整した高炉6において、各
支管風量が均一な風量で送風中に、第3図図示のように
一つの水蒸気吹き込み量制御弁5の開度を全閉(開度0
%)から開度50%に開操作して水蒸気を吹き込み送風湿
分を増加して、その送風支管2に設けた支管風量計3で
支管風量を実測したところ、水蒸気を吹き込み後支管風
量が増加すること、即ち羽口1よりの送風湿分を増加す
ることにより、その羽口1前の炉内通気性が即効的に改
善されることを知見した。
The inventors of the present invention carried out the water spray conditioning with the cold air tube and connected a single hot air tube to the annular tube, and provided 27 tuyere provided at equal intervals in the furnace circumferential direction as shown in FIG. A branch pipe air flow meter 3 and a steam injection nozzle 4 are provided for each of the 27 blower branch pipes 2 connected to 1, and a steam injection amount control valve 5 having the valve opening degree-flow rate characteristics shown in FIG. , Each tuyere 1
If the air permeability in the previous furnace is uniform, the amount of air blown from each tuyere 1 in a state in which steam is not blown in at a uniform opening of each steam blowing amount control valve 5, that is, in a fully closed state (opening 0%). In the blast furnace 6 in which the diameters of the tuyere 1 are adjusted so as to be uniform, the opening of one steam blowing amount control valve 5 is fully adjusted as shown in FIG. Closed (opening 0
%) To open the opening to 50% to increase the moisture content by blowing steam and measure the branch air flow rate with the branch pipe air flow meter 3 installed in the blower branch pipe 2, and the branch pipe air volume increases after the steam is blown. It has been found that the air permeability in the furnace in front of the tuyere 1 is immediately improved by doing so, that is, by increasing the amount of moisture sent from the tuyere 1.

水蒸気吹き込み量制御弁5を開操作して羽口1よりの送
風湿分を増加することにより、その羽口1前の装入物の
通気性が即効的に改善されるメカニズムは明確ではない
が、羽口1よりの送風湿分が増加すると、レースウェイ
内の粉コークスの水性ガス反応(H2O+C→H2+CO)が
促進され、レースウェイ内のコークス粉率が減少するた
めであると考えられる。
It is not clear the mechanism by which the air permeability of the charging material in front of the tuyere 1 is immediately improved by opening the water vapor injection control valve 5 to increase the amount of moisture sent from the tuyere 1. This is because when the amount of blast moisture from the tuyere 1 increases, the water gas reaction (H 2 O + C → H 2 + CO) of the powder coke in the raceway is promoted, and the coke powder ratio in the raceway decreases. Conceivable.

また本発明者等は上記高炉6において、上記水蒸気を水
に変更して、水吹き込みによって一つの羽口より炉内へ
送風される送風湿分を増加した結果、送風湿分を増加し
た羽口前の炉内通気性が即効的に改善されることも確認
した。
In addition, the present inventors changed the steam to water in the blast furnace 6 and increased the blast moisture that is blown into the furnace from one tuyere by blowing water, and as a result, the tuyere that increased the blast moisture content. It was also confirmed that the air permeability in the previous furnace was immediately improved.

尚、上記水又は水蒸気吹き込み量制御弁の設定開度と
は、例えば環状管に単一の熱風管が接続され、炉内円周
方向の通気性が均一であれば、各羽口からの送風量が均
一となるように各羽口の口径を調節すると共に冷風管で
送風湿分を所定湿分に調整するようにした高炉において
は、例えば全閉、即ち開度0%である。
Incidentally, the set opening of the water or steam injection amount control valve means, for example, if a single hot air tube is connected to an annular tube and the air permeability in the circumferential direction of the furnace is uniform, the air flow from each tuyere is reduced. In a blast furnace in which the caliber of each tuyere is adjusted so that the air volume becomes uniform and the blast moisture is adjusted to a predetermined humidity by a cold air tube, for example, it is fully closed, that is, the opening is 0%.

また例えば上記冷風管での送風調湿に代えて上記各水又
は水蒸気吹き込みノズルよりの水又は水蒸気吹込みのみ
で送風調湿するようにした上記高炉においては、上記所
定湿分にするに必要な弁開度である。
Further, for example, in the blast furnace in which the air conditioning is controlled only by blowing water or steam from the water or steam blowing nozzles in place of the air conditioning in the cold air tube, it is necessary to set the predetermined humidity. It is the valve opening.

また特開昭48−39122号公報又は特公昭57−52923号公報
で提案される送風設備を有して、送風設備上の各羽口か
らの送風量の不均一を解消した上記高炉においては、冷
風管で送風湿分を所定湿弁に調整するようにした場合、
上記水又は水蒸気吹き込み量制御弁の設定開度とは、例
えば全閉、即ち開度0%であり、各水又は水蒸気吹き込
みノズルよりの水又は水蒸気吹込みのみで送風調湿する
ようにした場合、上記所定湿分にするに必要な弁開度で
ある。
Further, in the above-mentioned blast furnace, which has a blower facility proposed in JP-A-48-39122 or JP-B-57-52923, the unevenness of the blown amount from each tuyere on the blower is eliminated. When the blast moisture is adjusted to the specified humidity valve with a cold air tube,
The set opening degree of the water or steam injection amount control valve is, for example, fully closed, that is, the opening degree is 0%, and the case where the air and humidity are adjusted only by blowing water or steam from each water or steam injection nozzle Is the valve opening required to achieve the above-mentioned predetermined humidity.

更に、上記送風支管の設定風量としては、例えば上記高
炉の総送風量を上記高炉の羽口数で割った論理平均風
量、或は(1−α)×論理平均風量(但しα<1,αは上
記高炉操業を安定維持することができる論理平均風量よ
りの減少風量によって経験的に決定する)等を採用する
ものである。
Further, as the set air flow rate of the blower branch pipe, for example, the total air flow rate of the blast furnace divided by the number of tuyere of the blast furnace, or a logical average air flow rate (1-α) × logical average air flow (where α <1, α is The blast furnace operation can be stably maintained by empirically determining the reduced air flow rate from the theoretical average air flow rate).

(実施例) 以下本発明の高炉操業方法を一実施例に基づき詳細に説
明する。
(Example) Hereinafter, the blast furnace operating method of the present invention will be described in detail based on an example.

冷風管で送風湿分36(g/Nm3)に散水調湿を行うと共に
環状管に単一の熱風管が接続され、第1図図示のように
炉周方向に等間隔で設けられた27本の羽口1と接続する
27本の送風支管2毎に、支管風量計3、水蒸気吹き込み
ノズル4を設け、上記ノズル4毎に第2図の弁開度〜流
量特性を有する水蒸気吹き込み量制御弁5を設け、各水
蒸気吹き込み量制御弁5の均一な開度、例えば全閉(開
度0%)で、各羽口1からの送風量が均一となるように
各羽口1の口径を調整した総送風量4050(Nm3/min)
〔論理平均風量150(Nm3/min)〕の高炉5において、例
えば第4図、第6図の円周方向の水蒸気吹き込み量制御
弁開度分布(以下、円周方向弁開度分布と略す)の如く
各水蒸気吹き込み量制御弁5の均一な設定開度、即ち全
閉(開度0%)で送風中、上記支管風量計4群で支管風
量(Nm3/min)を定期的に、例えば20min毎に検出し、第
5図、第7図の如き円周方向の支管風量分布(以下、円
周方向支管風量分布と略す)を検出する。
A cold air tube was used to control the water content of the blast with a humidity of 36 (g / Nm 3 ), and a single hot air tube was connected to the annular tube. Connect with tuyere 1 of the book
A branch pipe air flow meter 3 and a steam blowing nozzle 4 are provided for each of the 27 blow branch pipes 2, and a steam blowing amount control valve 5 having the valve opening-flow rate characteristics shown in FIG. With a uniform opening of the volume control valve 5, for example, fully closed (opening 0%), the air volume from each tuyere 1 is adjusted so that the air volume from each tuyere 1 is uniform. 3 / min)
In the blast furnace 5 having a [logical average air flow rate of 150 (Nm 3 / min)], for example, the distribution of the steam injection amount control valve opening in the circumferential direction in FIGS. 4 and 6 (hereinafter abbreviated as the circumferential valve opening distribution) ), The air flow rate (Nm 3 / min) is periodically adjusted by the four groups of branch pipe anemometers while the air is blown at a uniformly set opening of each steam blowing amount control valve 5, that is, at a fully closed position (opening 0%). For example, it is detected every 20 minutes, and the branch pipe air flow distribution in the circumferential direction as shown in FIG. 5 and FIG.

尚、上記第4〜7図及び後述する第8〜13図図示の分布
図において、1〜27は高炉5の円周方向の羽口及び送風
支管No.を表示している。また第4,6,8,10,12図の円周方
向弁開度分布図において、0,50,100は弁開度(%)を示
し、第5,7,9,11,13図の円周方向支管風量分布図におい
て、100,150,200は支管風量(Nm3/min)を示す。
In the distribution diagrams shown in FIGS. 4 to 7 and FIGS. 8 to 13, which will be described later, 1 to 27 indicate the tuyere and blast branch pipe numbers of the blast furnace 5 in the circumferential direction. In the circumferential valve opening distribution charts in Figures 4, 6, 8, 10, and 12, 0, 50, and 100 indicate the valve opening (%), and the circumferences in Figures 5, 7, 9, 11, and 13 In the directional branch airflow distribution map, 100, 150, 200 indicate the branch airflow (Nm 3 / min).

更に以下に詳述する実施例では、設定風量として〔(1
−α)×論理平均風量〕を採用し、上記αとしてα=0.
03を採用している。また各送風支管風量が〔(1±α)
×論理平均風量〕であれば、円周方向支管風量が均一で
あり、炉内円周方向の通気性が均一であると判断するも
のである。
Further, in the embodiment described in detail below, the set air volume is [(1
−α) × logical average air volume], and α = 0.
03 is adopted. In addition, the air volume of each blast branch pipe is [(1 ± α)
X logical average air volume], it is judged that the circumferential branch pipe air volume is uniform and the air permeability in the furnace circumferential direction is uniform.

今、第4図の円周方向弁開度分布の如く全水蒸気吹き込
み量制御弁5が設定開度で、第5図の円周方向支管風量
分布の如く円周方向支管風量が均一で炉内円周方向の通
気性が均一であったものが、コークス、鉱石類の粒度偏
析、原燃料性状の不均一、炉体損傷によるプロフィール
の悪化等の外乱により第4図と同じ設定弁開度分布(第
6図参照)下で、第7図の円周方向支管風量分布の如く
No.2〜9の支管2及び羽口1の風量が設定風量より減少
して、第7図の如く円周方向支管風量の不均一が検出さ
れ、炉内円周方向の通気性の不均一が検出されると、N
o.2〜9の送風支管2の水蒸気吹き込みノズル4の水蒸
気吹き込み量制御弁5の弁開度を第8図の如く設定開度
より増加して、No.2〜9の支管2、羽口1よりの送風湿
分を増加する。このNo.2〜9の送風支管2の水蒸気吹き
込みノズル4の水蒸気吹き込み量制御弁5の弁開度の設
定開度よりの増加操作によるNo.2〜9の送風支管2、羽
口1よりの炉内送風湿分の増加によってNo.2〜9の羽口
1前の炉内通気性が改善され、第8図と同じ弁開度分布
(第10図参照)下で、第9図から第11図の如くNo.2〜9
の送風支管2及び羽口1の風量が、各送風支管2の均一
な設定風量及び理論平均風量150(Nm3/min)に向かって
回復する このようにNo.2〜9の送風支管2の水蒸気吹き込みノズ
ル4の水蒸気吹き込み量制御弁5の弁開度の設定開度よ
りの増加操作によるNo.2〜9の送風支管2、羽口1より
の炉内送風湿分の増加によってNo.2〜9の羽口1前の炉
内通気性が改善され、第8図と同じ弁開度分布(第10図
参照)下で、第9図から第11図の如くNo.2〜9の送風支
管2及び羽口1の風量が設定風量及び論理平均風量150
(Nm3/min)に向かって回復すると、第12図の如くNo.2
〜9の送風支管2の水蒸気吹き込みノズル4の水蒸気吹
き込み量制御弁5の弁開度を設定開度、即ち全閉に戻
し、次いで支管風量計3群で支管風量(Nm3/min)を検
出し、円周方向の支管風量分布を検出する。この支管風
量分布に基づき、炉内円周方向の通気性の均一性を判断
し、第13図の円周方向支管風量分布の如く円周方向支管
風量の均一性が確保され、炉内円周方向の通気性が均一
であると判断させるまで、設定風量以下の送風支管2の
水蒸気吹き込みノズル4の水蒸気吹き込み量制御弁5の
弁開度の設定開度よりの増加操作乃至設定開度への復帰
操作を繰り返し実施する。
Now, as shown in the circumferential valve opening distribution of FIG. 4, the total steam injection amount control valve 5 is at the set opening, and the circumferential branch pipe air amount is uniform as in the circumferential branch pipe air amount distribution of FIG. Even though the air permeability in the circumferential direction was uniform, the set valve opening distribution was the same as in Fig. 4 due to disturbances such as segregation of coke and ore particles, non-uniformity of raw fuel properties, and deterioration of profile due to damage to the furnace body. (See Fig. 6) Below, like the circumferential branch pipe air flow distribution in Fig. 7.
The air volume of branch pipes 2 and tuyeres 1 of Nos. 2 to 9 decreased from the set air volume, and non-uniformity of circumferential branch pipe air volume was detected as shown in Fig. 7, and air permeability in the circumferential direction of the furnace was non-uniform. Is detected, N
o.2-9, the valve opening of the steam injection amount control valve 5 of the steam injection nozzle 4 of the blower branch pipe 2 is increased from the set opening as shown in FIG. Increase the blast moisture above 1. No. 2 to 9 blower branch pipes 2 and tuyere 1 are operated by increasing the opening degree of the steam blown amount control valve 5 of the steam blow nozzle 4 of the No. 2 to 9 blower branch pipes 2. Due to the increase in the amount of blast moisture in the furnace, the in-furnace air permeability in front of tuyere 1 of Nos. 2 to 9 was improved, and from Fig. 9 to Fig. 9 under the same valve opening distribution as Fig. 8 (see Fig. 10). No.2 ~ 9 as shown in Fig. 11
The air volume of the blast branch pipe 2 and the tuyere 1 recovers toward the uniform set air volume and the theoretical average air volume of 150 (Nm 3 / min) of each blast branch pipe 2 in this way. No.2 due to increase in the amount of moisture blown in the furnace from No.2-9 blower branch pipes 2 and tuyere 1 by the operation of increasing the valve opening of the steam injection amount control valve 5 of the steam injection nozzle 4 No.2 to 9 blows as shown in Fig. 9 to Fig. 11 under the same valve opening distribution as Fig. 8 (see Fig. 10) with improved air permeability in front of tuyere 1 The air volume of branch pipe 2 and tuyere 1 is set air volume and logical average air volume of 150
When recovering toward (Nm 3 / min), No. 2 as shown in Fig. 12
~ 9 of the steam blowing nozzle 4 of the blow-off branch pipe 2 to return the valve opening of the steam blowing amount control valve 5 to the set opening, that is, fully closed, and then detect the branch pipe air volume (Nm 3 / min) with the branch pipe air flow meter 3 group Then, the distribution flow amount of the branch pipe in the circumferential direction is detected. Based on this branch pipe airflow distribution, the uniformity of the air permeability in the circumferential direction of the furnace is judged, and the uniformity of the circumferential branch pipe airflow is ensured as in the circumferential branch pipe airflow distribution of Fig. 13. Until it is judged that the air permeability in the direction is uniform, the operation of increasing the valve opening of the steam blowing amount control valve 5 of the steam blowing nozzle 4 of the blower branch pipe 2 of the set air volume or less to the set opening or to the set opening Repeat the return operation.

第13図の円周方向支管風量分布の如く円周方向支管風量
の均一性が確保され、炉内円周方向の通気性の均一性が
確保されると、第12図の如く全水蒸気吹き込み量制御弁
5の弁開度を設定開度(全閉)としたまま送風を行い、
支管風量計3群で支管風量(Nm3/min)を定期的に検出
し、円周方向の支管風量分布を検出する。
If the uniformity of the circumferential branch pipe airflow is ensured as shown in the circumferential branch pipe airflow distribution in Fig. 13 and the air permeability in the circumferential direction of the furnace is also ensured, the total amount of steam injected is as shown in Fig. 12. Air is blown with the valve opening of the control valve 5 kept at the set opening (fully closed),
The tributary air flow meter (group 3 ) regularly detects the tributary air flow (Nm 3 / min) to detect the tributary air flow distribution in the circumferential direction.

次に具体的な実施結果について述べると、全水蒸気吹き
込み量制御弁5の開度が設定開度(全閉=開度0%)下
で、支管風量計3群の支管風量(Nm3/min)を20min毎に
検出し、円周方向の支管風量分布を検出し、円周方向の
支管風量分布が、第5図図示の如く均一で炉内円周方向
の通気性が均一であったものが第7図図示の如く不均一
となったことが検出された時、第8図の如くNo.2〜9の
全水蒸気吹き込み量制御弁5の弁開度を設定開度より増
加操作し、弁開度増加操作後、第8,10図の弁開度分布で
送風を継続し、第9図の支管風量分布を経て、弁開度増
加操作5時間後、第11図の支管風量分布になった時、第
12図の如くNo.2〜9の水蒸気吹き込み量制御弁5の弁開
度を設定開度へ復帰操作したところ、第13図の如く円周
方向の支管風量分布を均一にして、炉内円周方向の通気
性を均一にすることができた。即ち、炉内円周方向の通
気性の不均一の検出後、5時間の短時間で即効的に炉内
円周方向の通気性を均一にすることができた。
Next, the specific implementation results will be described. When the opening of the total steam injection amount control valve 5 is below the set opening (fully closed = 0% opening), the branch pipe air flow rate of the three groups of branch pipe anemometers (Nm 3 / min ) Is detected every 20 minutes to detect the distribution flow amount of the branch pipe in the circumferential direction, and the distribution flow amount of the branch pipe in the circumferential direction is uniform as shown in FIG. 5 and the air permeability in the circumferential direction of the furnace is uniform. Is detected as shown in FIG. 7, it is operated to increase the valve opening of the total steam injection amount control valves 5 of Nos. 2 to 9 as shown in FIG. After the valve opening increase operation, air is continuously blown with the valve opening distribution shown in Figs. 8 and 10. After the branch pipe air volume distribution shown in Fig. 9, 5 hours after the valve opening increase operation, the branch pipe air volume distribution shown in Fig. 11 is obtained. When it becomes
As shown in Fig. 12, when the valve opening of No. 2 to 9 steam injection control valve 5 was returned to the set opening, the branch pipe air flow distribution in the circumferential direction was made uniform as shown in Fig. 13, and The air permeability in the circumferential direction could be made uniform. That is, after the non-uniformity of the air permeability in the circumferential direction in the furnace was detected, the air permeability in the circumferential direction in the furnace could be made uniform immediately in a short time of 5 hours.

(発明の効果) 以上詳述したように、本発明の高炉操業方法によれば、
炉内円周方向の不均一を即効的に均一にして高炉操業を
安定維持することができる。
(Effects of the Invention) As described in detail above, according to the blast furnace operating method of the present invention,
The non-uniformity in the circumferential direction in the furnace can be promptly made uniform and the blast furnace operation can be stably maintained.

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

第1〜3図(イ)(ロ)は、本発明法の基礎となる送風
湿分増加による羽口前の炉内通気性の即効的改善特性の
説明図、第4〜13図は本発明の高炉操業方法の一実施例
の説明図である。 1……羽口 2……送風支管 3……支管風量計 4……水蒸気吹き込みノズル 5……水蒸気吹き込み量制御弁 6……高炉
FIGS. 1 to 3 (a) and (b) are explanatory views of the effect of immediately improving the air permeability in the furnace in front of the tuyere by increasing the blast moisture which is the basis of the method of the present invention, and FIGS. 4 to 13 show the present invention. It is explanatory drawing of one Example of the blast furnace operating method of this. 1 …… Tuyere 2 …… Blast branch pipe 3 …… Branch pipe air flow meter 4 …… Steam injection nozzle 5 …… Steam injection control valve 6 …… Blast furnace

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭51−24515(JP,A) 特開 昭58−58205(JP,A) 特開 昭58−133308(JP,A) 特開 昭54−110906(JP,A) ─────────────────────────────────────────────────── ─── Continuation of front page (56) Reference JP-A-51-24515 (JP, A) JP-A-58-58205 (JP, A) JP-A-58-133308 (JP, A) JP-A-54- 110906 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】羽口に接続された送風支管毎に支管風量
計、水又は水蒸気吹き込みノズルを設け、上記ノズル毎
に水又は水蒸気吹き込み量を制御する水又は水蒸気吹き
込み量制御弁を設けた高炉において、上記支管風量計群
の風量を定期的に検出し、各送風支管均一な設定風量よ
り風量が減少した送風支管の水又は水蒸気吹き込み量制
御弁の開度を、各水又は水蒸気吹き込み量制御弁均一な
設定開度より増加して水又は水蒸気を上記ノズル、送風
支管、羽口を介して炉内へ吹き込み、上記設定風量より
風量が減少した送風支管に接続された羽口前の炉内通気
性を改善し、上記水又は水蒸気吹き込み量制御弁の開度
を上記設定開度に戻すことを特徴とする高炉操業方法。
1. A blast furnace in which a branch pipe air flow meter, a water or steam blowing nozzle is provided for each blower branch pipe connected to a tuyere, and a water or steam blowing amount control valve for controlling the amount of water or steam blowing is provided for each nozzle. In, the air flow rate of the branch pipe air flow meter group is detected periodically, and the opening of the water or water vapor injection amount control valve of the air flow tributary pipe in which the air flow amount is reduced from the uniform air flow amount of each air blow tributary pipe is controlled by each water or water vapor injection amount. In the furnace in front of the tuyere connected to the blast tributary whose air volume has decreased below the set air volume, by blowing water or steam into the furnace through the nozzle, blast tributary, and tuyere to increase beyond the uniform set opening. A method for operating a blast furnace, characterized by improving breathability and returning the opening of the water or steam injection control valve to the set opening.
JP61262697A 1986-11-06 1986-11-06 Blast furnace operation method Expired - Lifetime JPH0776371B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61262697A JPH0776371B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61262697A JPH0776371B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Publications (2)

Publication Number Publication Date
JPS63118006A JPS63118006A (en) 1988-05-23
JPH0776371B2 true JPH0776371B2 (en) 1995-08-16

Family

ID=17379338

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61262697A Expired - Lifetime JPH0776371B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Country Status (1)

Country Link
JP (1) JPH0776371B2 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610364B2 (en) * 1973-01-09 1981-03-07
JPS5124515A (en) * 1974-08-23 1976-02-27 Nippon Steel Corp KOROSOGYOHOHO
JPS5313325A (en) * 1976-07-21 1978-02-06 Mitsubishi Electric Corp Connection method between information processing unit and peripheral device
JPS5858205A (en) * 1981-09-30 1983-04-06 Sumitomo Metal Ind Ltd Operating method for blast furnace
JPS58133308A (en) * 1982-02-03 1983-08-09 Sumitomo Metal Ind Ltd Operation of shaft furnace
JPS60114511A (en) * 1983-11-25 1985-06-21 Sumitomo Metal Ind Ltd Method for controlling flow rate of blast furnace

Also Published As

Publication number Publication date
JPS63118006A (en) 1988-05-23

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