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JPH0776370B2 - Blast furnace operation method - Google Patents
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JPH0776370B2 - Blast furnace operation method - Google Patents

Blast furnace operation method

Info

Publication number
JPH0776370B2
JPH0776370B2 JP61262696A JP26269686A JPH0776370B2 JP H0776370 B2 JPH0776370 B2 JP H0776370B2 JP 61262696 A JP61262696 A JP 61262696A JP 26269686 A JP26269686 A JP 26269686A JP H0776370 B2 JPH0776370 B2 JP H0776370B2
Authority
JP
Japan
Prior art keywords
branch pipe
air
air flow
valve opening
furnace
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
JP61262696A
Other languages
Japanese (ja)
Other versions
JPS63118005A (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 JP61262696A priority Critical patent/JPH0776370B2/en
Publication of JPS63118005A publication Critical patent/JPS63118005A/en
Publication of JPH0776370B2 publication Critical patent/JPH0776370B2/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、送風支管毎に支管風量制御弁及び支管風量計
を設けた高炉の操業方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for operating a blast furnace in which a branch pipe air flow control valve and a branch pipe air flow meter are provided for each blast branch pipe.

(従来の技術) 高炉操業を安定させるためには、炉内円周方向での炉内
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 circumferentially 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、冷風を1000〜1200℃の熱風となし熱風
管、環状管を通つて各送風支管を介して各羽口より行
う。しかして環状管と熱風炉は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
つても、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つてくる。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)によつて解消できる。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
向に沿つ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)ことによつても
解消できる。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
は炉内円周方向の通気性を示し、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。
However, in general, air is blown into the furnace of a blast furnace by sending cold air from a blower to a hot air stove, and sending cool air from the tuyeres through the air blow pipes through the hot air pipes with 1000 to 1200 ° C. and without hot air pipes and annular pipes. However, since the annular tube and the hot-air stove are usually connected by a single hot-air tube, even if the air permeability in the circumferential direction in the furnace is uniform, the tuyere near the connecting part of the hot-air tube and the far away tuyere Then, the amount of air blown into the furnace varies. 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). No. 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). Alternatively, the blast branch pipe group is divided into multiple blast branch pipe groups along the blast furnace circumferential direction, this blast branch pipe group is connected to the distribution pipes provided for each blast branch pipe group, and each distribution pipe is looped through a communication pipe. It can also be solved by connecting to a pipe and installing a flow control valve in each communication pipe (Japanese Patent Publication No. 57-52923). Incidentally, if the air permeability in the circumferential direction in the furnace is uniform, in the blast furnace that is configured so that the amount of air blown from each tuyere is uniform as described above and that a branch pipe airflow meter is provided for each blown branch pipe, The branch pipe air volumes measured by the branch pipe airflow meters show the air permeability in the furnace circumferential direction, and the branch pipe airflow groups measured by the branch pipe airflow meter group show the air permeability in the furnace circumferential direction.

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
プロフイールの悪化等が要因となつて生じる。
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つて解消できるが、装入
物分布のアクシヨンを取つたあと、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 the charge distribution has been taken. 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、上記送風支管毎に支管風量制御弁及び支管風
量計を設けた高炉における新知見である特定羽口の送風
量減少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 utilizes immediate improvement characteristics of in-furnace air permeability in front of a specific tuyere, which is a new finding in a blast furnace in which a branching airflow control valve and a branching airflow meter are provided for each of the above blasting branch pipes. Thus, the present invention provides a method for operating a blast furnace in which the non-uniformity of air permeability in the circumferential direction of the furnace can be promptly made uniform to stably maintain the operation of the blast furnace.

(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制御弁及び支管
風量計を設けた高炉において、上記支管風量制御弁群の
設定弁開度下の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
支管の支管風量制御弁の弁開度を設定弁開度より減少
し、送風量を減少して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、上記支
管風量制御弁の弁開度を設定弁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 air flow control valve and a branch pipe air flow meter for each blast branch pipe connected to the tuyere, the air flow rate of the branch pipe air flow meter group under the set valve opening of the branch pipe air flow control valve group is periodically detected. , Each blast branch pipe has an air volume that is less than the set air volume.The air flow rate control valve of the blast branch pipe has a valve opening that is smaller than the set valve opening, and the air volume has been reduced to connect to a blast tube that has a smaller air volume than the set air volume. The method for operating a blast furnace is characterized by improving the air permeability in the furnace before the tuyere and returning the valve opening of the branch pipe air flow control valve to the set valve opening.

本発明者等は、第1図図示のように環状管6に単一の熱
風管7が接続され、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、第2図の弁
開度〜流量比特性を有する支管風量制御弁3及び支管風
量計4を設け、各羽口1前の炉内通気性が均一であれ
ば、各支管風量制御弁3の弁開度の等開度下で、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5において、全支管風量制御弁3の弁開度全
開(弁開度100%)で送風中に、第3図図示のように一
つの支管風量制御弁3の弁開度を減少(弁開度30%)し
て、弁開度を減少操作した送風支管2の支管風量(弁開
度を減少し操作した送風支管2に接続された羽口1から
炉内への送風量)を、その送風支管2に設けた支管風量
計4で実測したところ、支管風量制御弁3の弁開度減少
操作後、一旦支管風量は減少するが、その後支管風量が
増加すること、即ち支管風量制御弁3の弁開度を減少し
て羽口1よりの送風量を減少することにより、その羽口
1前の炉内通気性が数時間で即効的に改善されることを
知見した。
The inventors of the present invention have shown that, as shown in FIG. 1, a single hot air tube 7 is connected to the annular tube 6, and 27 air blowers connected to 27 tuyere 1 provided at equal intervals in the furnace circumferential direction. Each branch pipe 2 is provided with a branch pipe air flow rate control valve 3 and a branch pipe air flow meter 4 having the valve opening-flow rate ratio characteristics shown in FIG. 2. If the in-furnace air permeability in front of each tuyere 1 is uniform, each branch pipe air flow rate is increased. In the blast furnace 5 in which the diameter of each tuyere 1 is adjusted so that the amount of air blown from each tuyere 1 is uniform under the same opening degree of the control valve 3, all the branch pipe air volume control valves 3 are opened. While the air is being blown at full opening (valve opening 100%), the valve opening of one branch pipe air flow control valve 3 is decreased (valve opening 30%) as shown in Fig. 3 to decrease the valve opening. The amount of branch air of the blown branch pipe 2 (the amount of air blown from the tuyere 1 connected to the operated blower branch pipe 2 into the furnace) was measured by the branch pipe air flow meter 4 installed in the blower branch pipe 2. By the way After the operation of decreasing the valve opening of the pipe air volume control valve 3, the branch pipe air volume temporarily decreases, but thereafter the branch pipe air volume increases, that is, the valve opening of the branch pipe air volume control valve 3 decreases and the amount of air blown from the tuyere 1 It was found that the air permeability in the furnace before the tuyere 1 was improved immediately within a few hours by decreasing

支管風量制御弁3の弁開度を減少して羽口1よりの送風
量を減少することにより、その羽口1前の炉内通気性が
即効的に改善されるメカニズムは明確ではないが、支管
風量、羽口送風量が減少すると羽口先風速が減少し、レ
ースウエ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。尚上記支管風量制御弁群の設定弁開度とは、
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、各支管風量制御弁の等弁開度下で、
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
調整した高炉においては、例えば全開、即ち弁開度100
%である。また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支管風量制御
弁の弁開度を設定した高炉5おいては、上記のように設
定した弁開度である。
Although the mechanism by which the air permeability in the furnace in front of the tuyere 1 is immediately improved by reducing the valve opening of the branch pipe air flow control valve 3 to reduce the air flow from the tuyere 1, is not clear, It is considered that this is because when the branch air volume and the tuyere air flow rate decrease, the tuyere tip wind speed decreases and the coke powder ratio in the raceway decreases. The set valve opening of the branch pipe air flow control valve group is
A single hot air pipe is connected to the annular pipe, and if the air permeability in the circumferential direction in the furnace is uniform, under equal valve opening of each branch pipe air flow control valve,
In a blast furnace in which the diameter of each tuyere is adjusted so that the amount of air blown from each tuyere is uniform, for example, fully open, that is, valve opening 100
%. If the air permeability in the circumferential direction in the furnace is uniform,
In the blast furnace 5 in which the valve opening of each branch pipe air flow control valve is set so that the air flow from each tuyere is uniform, the valve opening is set as described above.

また特公昭48−39122号公報又は特公昭57−52923号公報
で提案されてい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、且つ羽口に接続され
た送風支管毎に支管風量制御弁及び支管風量計を設けた
高炉においては、例えば全開、即ち弁開度100%であ
る。
In addition, by having a ventilation system proposed in Japanese Patent Publication No. 48-39122 or Japanese Patent Publication No. 57-52923, it eliminates the unevenness of the amount of air blown from each tuyere on the ventilation equipment, and In a blast furnace in which a branch pipe air flow control valve and a branch pipe air flow meter are provided for each connected blower branch pipe, for example, it is fully opened, that is, the valve opening is 100%.

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つた論理平均風
量、或いは〔(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つて決定する)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, a total average air flow rate of the blast furnace divided by the number of tuyere of the blast furnace, or [(1-α) × logical average air flow rate] (where α <1,
α is determined according to the reduced air flow rate from the logical average air flow rate that can maintain stable operation of the blast furnace).

(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.

第1図図示のように環状管6に単一の熱風管7が接続さ
れ、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、第2図の弁開度〜流量比特
性を有する支管風量制御弁3及び支管風量計4を設け、
各支管風量制御弁3の均一な弁開度、例えば全開(弁開
度100%)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図の円周方向の支管風量制御弁開度分
布(以下、円周方向弁開度分布と略す)の如く各支管風
量制御弁3の均一な設定弁開度、即ち全開(弁開度100
%)で送風中に、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。
As shown in FIG. 1, a single hot air tube 7 is connected to the annular tube 6, and for each of the 27 blower branch tubes 2 connected to the 27 tuyeres 1 provided at equal intervals in the furnace circumferential direction, The branch pipe air volume control valve 3 and the branch pipe air flow meter 4 having the valve opening-flow rate ratio characteristics shown in FIG.
The total air flow rate in which the diameter of each tuyere 1 is adjusted so that the air flow rate from each tuyere 1 is uniform when the air flow rate of each tributary airflow control valve 3 is uniform, for example, fully open (100% valve opening). 4050 (Nm 3 / min)
In the blast furnace 5 having a [logical average air flow rate of 150 (Nm 3 / min)], for example, circumferential branch pipe air flow control valve opening distributions in FIGS. 4 and 6 (hereinafter, abbreviated as circumferential valve opening distributions) As described above, each branch pipe air flow control valve 3 has a uniform set valve opening, that is, fully opened (valve opening 100
%), The branch air flow rate (Nm 3 /
min) is periodically detected, for example, every 20 minutes, and a branch pipe air flow distribution in the circumferential direction as shown in FIGS. 5 and 7 (hereinafter abbreviated as circumferential branch pipe air flow distribution) is detected.

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支管風量制御
弁3が均一な設定弁開度で、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
通気性が均一であつたものが、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イー
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、No.2〜9の送風支管2の支管風量制御弁3の弁開度
を第8図の如く設定弁開度より減少して、一旦No.2〜9
の送風支管2及び羽口1の風量を第9図の如く第7図よ
りも更に減少する。このNo.2〜9の送風支管2の支管風
量制御弁3の弁開度の設定弁開度よりの減少操作による
No.2〜9の送風支管2、羽口1よりの炉内送風量の減少
によつて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
が設定風量及び理論平均風量150(Nm3/min)に向かつて
回復する。
Now, as shown in the circumferential valve opening distribution in FIG. 4, all branch pipe air flow control valves 3 have a uniform set valve opening, and in the circumferential branch pipe air flow distribution in FIG. 5, the circumferential branch pipe air amounts are uniform. The same setting valve as in Fig. 4 was used due to disturbances such as coke, ore particle size segregation, non-uniformity of raw fuel properties, deterioration of profile due to damage to the furnace body, etc. Under the opening distribution (see FIG. 6), the air volume of the branch pipes 2 and tuyere 1 of Nos. 2 to 9 is smaller than the set air volume as in the circumferential branch pipe air volume distribution of FIG. As described above, when the unevenness of the circumferential branch pipe airflow is detected and the unevenness of the air permeability in the circumferential direction of the furnace is detected, the valve opening degree of the branch pipe airflow control valve 3 of the blower branch pipes No. 2 to 9 is changed. As shown in FIG.
The air volume of the blast branch pipe 2 and the tuyere 1 is further reduced as shown in FIG. 9 as compared with FIG. Due to the operation of decreasing the valve opening of the branch pipe air volume control valve 3 of the blower branch pipe 2 of No. 2 to 9 from the set valve opening
Due to the decrease in the amount of air blown from the No. 2 to 9 blast branch pipes 2 and the tuyere 1, the in-furnace air permeability in front of the No. 2 to 9 tuyere 1 is improved,
Under the same valve opening distribution as in Fig. 8 (see Fig. 10), as shown in Fig. 9 to Fig. 11, the blower branch pipes 2 and tuyeres 1 of Nos. 2 to 9 have the set air volume and the theoretical average air volume of 150. Recovers to (Nm 3 / min) once.

このようにNo.2〜9の送風支管2の支管風量制御弁3の
弁開度の設定弁開度よりの減少操作によるNo.2〜9の送
風支管2、羽口1よりの炉内送風量の減少によつて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
び理論平均風量150(Nm3/min)に向かつて回復すると、
第12図の如くNo.2〜9の送風支管2の支管風量制御弁3
の弁開度を設定弁開度、即ち全開に戻し、次いで支管風
量計4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、炉内円周方法の通気性が均一であると判断され
るまで、設定風量以下の送風支管2の支管風量制御弁3
の弁開度の設定弁開度よりの減少操作乃至設定弁開度へ
の復帰操作を繰り返し実施する。
In this way, the blower branch pipes No. 2 to 9 and the tuyere 1 are fed into the furnace by the operation of decreasing the valve opening degree of the branch pipe air volume control valve 3 of the blower branch pipes No. 2 to 9 No.2 due to the reduction of air volume
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 When the air volume of the branch pipe 2 and the tuyere 1 once recovered toward the set air volume and the theoretical average air volume of 150 (Nm 3 / min),
As shown in FIG. 12, the branch pipe air flow control valve 3 of the blower branch pipes No. 2 to 9
The valve opening of is returned to the set valve opening, that is, fully opened, and then the branch pipe airflow meter (group 4) detects the branch pipe airflow (Nm 3 / min) to detect the branch pipe airflow distribution in the circumferential direction. Based on this branch airflow distribution,
By judging the uniformity of air permeability in the circumferential direction of the furnace, the uniformity of air flow in the circumferential branch pipe is ensured as shown in the distribution of air flow in the circumferential direction of the branch pipe in Fig. 13. Until it is determined that there is a set air flow, the branch air flow control valve 3 of the blower branch pipe 2
The operation of decreasing the valve opening from the set valve opening or the operation of returning to the set valve opening is repeatedly performed.

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図の如く全支管風量制御弁3の弁開
度を設定弁開度(全開としたまま送風を行い、支管風量
計4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 air flow is ensured as in the circumferential branch pipe air flow distribution in Fig. 13, and the air permeability in the circumferential direction of the furnace is also ensured, the total branch pipe air flow control is performed as shown in Fig. 12. Set the valve opening of valve 3 (The air is blown while the valve is fully opened, and the branch pipe airflow meter (Nm 3 / min) is periodically detected by the branch pipe airflow meter 4 group to detect the branch pipe airflow distribution in the circumferential direction. To do.

次に具体的な実施結果について述べると、全支管風量制
御弁3の弁開度が設定弁開度(全開=弁開度100%)下
で、支管風量計4群で支管風量(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つたものが第7図図示の如く不均一
となつたことが検出された時、設定風量より風量が減少
したNo.2〜9の送風支管2の支管風量制御弁3の弁開度
を第8図の如く設定弁開度より減少操作し、弁開度減少
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、弁開度減少操作6時間後、第11
図の支管風量分布になつた時、第12図の如くNo.2〜9の
送風支管2の支管風量制御弁3の弁開度を設定弁開度へ
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、6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 valve opening of the total branch air flow control valve 3 is under the set valve opening (fully open = valve opening 100%), the branch pipe air flow meter (Nm 3 / min) every 20 min to detect the distribution flow amount of the branch pipe in the circumferential direction. The distribution flow amount of the branch pipe in the circumferential direction was uniform as shown in Fig. 5, and the air permeability in the circumferential direction of the furnace was uniform. Fig. 8 shows the valve opening of the branch pipe air volume control valve 3 of the blower branch pipes No. 2 to 9 in which the air volume is reduced from the set air volume when it is detected that the air flow is uneven as shown in Fig. 7. As shown in Fig.8 and 10, the ventilation is continued with the valve opening distribution shown in Figs.8 and 10, and the valve opening decreasing operation is performed through the branch pipe air volume distribution shown in Fig.9. After hours, 11th
When the branch pipe air flow distribution shown in the figure is reached, as shown in FIG. 12, when the valve opening of the branch pipe air flow control valve 3 of the blower branch pipes No. 2 to 9 is returned to the set valve opening, as shown in FIG. It was possible to make the distribution of the branch pipe air flow in the circumferential direction uniform and to make the air permeability in the circumferential direction in the furnace 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 immediately made uniform in a short time of 6 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。
(Effects of the Invention) As described in detail above, according to the blast furnace operating method of the present invention,
The unevenness of the air permeability 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特定
羽口の送風量減少による特定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……支管風量制御弁 4……支管風量計 5……高炉 6……環状管 7……熱風管
FIGS. 1 to 3 (a) and (b) are explanatory views of the immediately effective improvement characteristics of the in-furnace air permeability before the specific tuyere due to the reduction of the air flow rate of the specific tuyere, which is the basis of the method of the present invention, and 4 to 13 The figure is an explanatory view of an embodiment of the blast furnace operating method of the present invention. 1 …… Tuyere 2 …… Blast branch pipe 3 …… Branch pipe air flow control valve 4 …… Branch pipe air flow meter 5 …… Blast furnace 6 …… Annular pipe 7 …… Hot air pipe

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭61−295309(JP,A) 特開 昭51−24515(JP,A) 特開 昭54−110906(JP,A) 特開 昭49−91906(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-61-295309 (JP, A) JP-A-51-24515 (JP, A) JP-A-54-110906 (JP, A) JP-A-49- 91906 (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制
御弁及び支管風量計を設けた高炉において、上記支管風
量制御弁群の設定弁開度下の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支管風量制御弁の弁開度を設定弁開
度より減少し、送風量を減少して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、上記支管風量制御弁の弁開度を設定弁開度に戻すこ
とを特徴とする高炉操業方法。
1. In a blast furnace in which a branch pipe air flow control valve and a branch pipe air flow meter are provided for each blast branch pipe connected to a tuyere, the air flow rate of the branch pipe air flow meter group under the set valve opening of the branch pipe air flow control valve group is set. Detected periodically, the air volume has decreased from the set air volume evenly for each blast branch pipe.The valve opening of the tributary air flow control valve of the blast tributary is reduced below the set valve opening, and the blast volume is reduced to decrease the air volume below the set air volume. A method for operating a blast furnace, characterized in that the air permeability in the furnace before the tuyere connected to the blower branch pipe is improved, and the valve opening of the branch pipe air flow control valve is returned to the set valve opening.
JP61262696A 1986-11-06 1986-11-06 Blast furnace operation method Expired - Lifetime JPH0776370B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61262696A JPH0776370B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61262696A JPH0776370B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Publications (2)

Publication Number Publication Date
JPS63118005A JPS63118005A (en) 1988-05-23
JPH0776370B2 true JPH0776370B2 (en) 1995-08-16

Family

ID=17379323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61262696A Expired - Lifetime JPH0776370B2 (en) 1986-11-06 1986-11-06 Blast furnace operation method

Country Status (1)

Country Link
JP (1) JPH0776370B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610364B2 (en) * 1973-01-09 1981-03-07
JPS5313325A (en) * 1976-07-21 1978-02-06 Mitsubishi Electric Corp Connection method between information processing unit and peripheral device
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
JPS63118005A (en) 1988-05-23

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