JP3978105B2 - Raw material charging method for blast furnace - Google Patents

Raw material charging method for blast furnace Download PDF

Info

Publication number
JP3978105B2
JP3978105B2 JP2002272584A JP2002272584A JP3978105B2 JP 3978105 B2 JP3978105 B2 JP 3978105B2 JP 2002272584 A JP2002272584 A JP 2002272584A JP 2002272584 A JP2002272584 A JP 2002272584A JP 3978105 B2 JP3978105 B2 JP 3978105B2
Authority
JP
Japan
Prior art keywords
raw material
upper flow
level
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
JP2002272584A
Other languages
Japanese (ja)
Other versions
JP2004107732A (en
Inventor
育野 山田
康次郎 園
真一 竹下
孝 肥田
剛 川崎
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 JP2002272584A priority Critical patent/JP3978105B2/en
Publication of JP2004107732A publication Critical patent/JP2004107732A/en
Application granted granted Critical
Publication of JP3978105B2 publication Critical patent/JP3978105B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Manufacture Of Iron (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、固定ホッパー下部にある貯留ホッパー内の原料堆積レベルを一定に保つことにより、原料落下軌跡の安定化を図ることができる高炉の原料装入方法に関するものである。
【0002】
【従来の技術】
【特許文献1】
特公昭63−39642号公報
【0003】
従来から、鉄鉱石およびコークスの各固定ホッパーからの原料を貯留ホッパーを介して炉内旋回シュートに供給し、該炉内旋回シュートの傾動および旋回により交互に炉内に装入分配するようにしたベルレス式高炉の原料装入方法が広く知られている。一方、高炉の繰業を安定的に維持するためには、炉内各位置における鉄鉱石の量とコークスの量の比や層状態を一定に保ち、炉内ガス流分布や炉熱分布等を均一にすることが重要である。
【0004】
そこで、本件出願人は炉内装入原料のレベルをフラットにし、炉径方向の粒度を炉径方向に段階的に変化させるようにした高炉の原料装入方法を開発し、特許文献1として示すように、先に特公昭63−39642号(特願昭60−67396号)として提案した。
しかしながら、本発明者が研究した結果、貯留ホッパーから炉内旋回シュートへ落下する原料の落下軌跡が鉄鉱石とコークスの層状態を均一化するのに大きな影響を与えることを見出した。即ち、貯留ホッパー内の原料堆積レベルが変動すると原料の落下軌跡が変化して、炉内に均一な原料の層を形成することができないという問題点があることを見出した。従って、貯留ホッパー内の原料堆積レベルを一定に保つための新たな技術の開発が望まれていた。
また、従来は上部流調ゲートの初期開度を経験的に求めた所定値に定めていたので、原料の粒度変化等により原料の溜まり具合が変化した場合には、貯留ホッパー内の原料堆積レベルの制御性にも悪影響が出るという問題点もあった。
【0005】
【発明が解決しようとする課題】
本発明は上記のような従来の問題点を解決して、固定ホッパー下部にある貯留ホッパー内の原料堆積レベルを一定に保つことにより、原料落下軌跡の安定化を図ることができ、更には原料の粒度変化等があっても次回の原料装入時には何ら影響を受けることなく原料堆積レベルを一定に保持しつつ原料を装入できる高炉の原料装入方法を提供することを目的として完成されたものである。
【0006】
【課題を解決するための手段】
上記の課題を解決するためになされた本発明の高炉の原料装入方法は、鉄鉱石およびコークスの各固定ホッパーの原料を貯留ホッパーを介して炉内旋回シュートに交互に供給し、該炉内旋回シュートの傾動および旋回により炉内に装入分配する高炉の原料装入方法において、前記固定ホッパー下部にある上部流調ゲートの開度を、各固定ホッパー毎に設定される各上部流調ゲート( 10a )、( 10b )のベース開度をそれぞれ(θ a )、(θ b )、および各固定ホッパー毎に設定される補正角度をそれぞれ(β a )、(β b とした場合に、所定のレベルになった時点で上部流調ゲートの開度を(θ a −β a )あるいは(θ b −β b とし、低いレベルになった時点で上部流調ゲートの開度を(θ a )あるいは(θ b に戻し、高いレベルになった時点で上部流調ゲートの開度を(θ a −2β a )あるいは(θ b −2β b とし、所定のレベルになった時点で(θ a −β a )あるいは(θ b −β b に戻すように調整して、1回の原料装入工程における全時間のうち、各原料の溜まり具合がいずれのレベルに属するかを時間に換算し定量化したデータを用いて、上部流調ゲートの平均開度を算出し、この値を基に次回の原料装入時における各固定ホッパーの上部流調ゲートの初期開度を決定することを特徴とするものである。
【0007】
【発明の実施の形態】
以下に、図面を参照しつつ本発明の好ましい実施の形態を示す。
図1において、 a は鉄鉱石の各固定ホッパー、 1b はコークスの固定ホッパー、2は高炉本体であり、前記固定ホッパーには鉄鉱石とコークスとが一定周期で入れ替えて投入されている。これらの各原料は、上部にあるベルトコンベア3および切替シュート4を通じて各固定ホッパー a 、1 bへ装入される。そして各固定ホッパー a 、1 bに貯留された鉄鉱石およびコークス原料は、貯留ホッパー5を介して炉内旋回シュート6に交互に供給され、該炉内旋回シュート6の傾動および旋回により炉内に装入分配されるものであり、以上の原料装入工程は従来のベルレス式高炉の原料装入方法と基本的に同じである。
【0008】
そして本発明においては、前記固定ホッパー下部にある上部流調ゲート10の開度を、貯留ホッパー5内に設置したレベル計7を基に原料の溜まり具合が一定となるように調整しつつ原料を装入するとともに、この時の上部流調ゲート10の平均開度を算出し、この値を基に次回の原料装入時における上部流調ゲート10の初期開度を決定するようにした点に特徴を有するものである。
【0009】
更に詳述すれば、貯留ホッパー5内には原料の溜まり具合を計測するレベル計7が設置されている。具体的には上下方向に3個のレベル計7、7、7(上からH、M、Lとする)が設置されており、レベル計を超えて原料が溜まった場合に各レベル計より信号が発せられ、1回の原料装入工程における全時間のうち、原料の溜まり具合がレベルL未満、レベルL〜M、レベルM〜H、レベルH以上の4段階のいずれに属するかを時間に換算し定量化するよう構成されている。
【0010】
そして、上記のように定量化した数値に基づいて、上部流調ゲート10の開度を調整し、原料の溜まり具合がレベルMの近辺を維持するように微調整する。
即ち、各上部流調ゲート10 a 、10 bのベース開度をそれぞれ(θ a )、(θ b とすると、レベルMになった時点で各上部流調ゲート10 a 、10 bの開度を(θ a −β a )あるいは(θ b −β b とする。ここで、β a 、β bは鉄鉱石、コークスの銘柄、および各固定ホッパー毎に設定される補正角度である。そして、レベルLになった時点で各上部流調ゲート10 a 、10 bの開度を(θ a )あるいは(θ b に戻す。また、レベルHになった時点で各上部流調ゲート10 a 、10 bの開度を(θ a −2β a )あるいは(θ b −2β b とし、レベルMになった時点で(θ a −β a あるいは(θ b −2β b に戻すようにして調整する。
なお、レベルM、Hを検出し上部流調ゲート10の開度を(θ a −β a )あるいは(θ b −β b )、(θ a −2β a )あるいは(θ b −2β b に制御して、一定時間経過後においてもレベルがL、Mに戻らない場合は、入力値異常として上部流調ゲート10の開度をベース開度(θ)に戻して再制御する。
【0011】
また、このように1回の原料装入工程における全時間のうち、原料の溜まり具合がいずれのレベルに属するかを時間に換算し定量化したデータを用いて、上部流調ゲートの平均開度を算出し、この値を基に次回の原料装入時における上部流調ゲートの初期開度を決定する。これにより、原料粒度の変化等による溜まり具合の変化があったとしても、上部流調ゲートの初期開度が適正値となっているため、次回の原料装入時に悪影響が出ることがなく、円滑な原料装入を実行することが可能となる。
なお、次回の原料装入時における上部流調ゲートの初期開度の決定は、具体的には1回の原料装入工程における全時間のうち、原料の溜まり具合がレベルL未満、レベルL〜M、レベルM〜H、レベルH以上の4段階のいずれに属するかを時間に換算し定量化した値をもとに、各レベルの時間割合を算出(全体を100とした場合の比率で算出)し、これに補正係数を掛けた数値の平均をとって平均レベルとする。そして、この平均レベルと比較してその±で補正を加え、上部流調ゲートの初期開度を決定するのである。
【0012】
このように、本発明では固定ホッパー下部にある上部流調ゲート10の開度を、貯留ホッパー5内に設置したレベル計7を基に原料の溜まり具合が一定となるように調整しつつ原料を装入するとともに、この時の上部流調ゲート10の平均開度を算出し、この値を基に次回の原料装入時における上部流調ゲート10の初期開度を決定するようにしたので、例えば原料の粒度に変化等があっても、貯留ホッパー内の原料堆積レベルは一定に保たれることとなる。この結果、原料を炉内旋回シュート6へ常に一定の条件で落下させることができるため、炉内各位置における鉄鉱石の量とコークスの量の比や層状態を一定に保つこととなり、炉内反応を一定にして安定した高炉繰業を確保できることとなる。
【0013】
【発明の効果】
以上の説明からも明らかなように、本発明は固定ホッパー下部にある貯留ホッパー内の原料堆積レベルを一定に保つことにより、原料落下軌跡の安定化を図ることができ、更には原料の粒度変化等があっても次回の原料装入時には何ら影響を受けることなく原料堆積レベルを一定に保持しつつ原料を装入できるものである。
よって本発明は従来の問題点を一掃した高炉の原料装入方法として、産業の発展に寄与するところは極めて大である。
【図面の簡単な説明】
【図1】本発明の実施の形態を示す正面図である。
【符号の説明】
a 鉄鉱石の固定ホッパー
b コークスの固定ホッパー
2 高炉本体
5 貯留ホッパー
7 レベル計
10 a 上部流調ゲート
10 b 上部流調ゲート
11 下部流調ゲート
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a raw material charging method for a blast furnace capable of stabilizing a raw material falling trajectory by keeping a raw material accumulation level in a storage hopper below a fixed hopper constant.
[0002]
[Prior art]
[Patent Document 1]
Japanese Patent Publication No. 63-39642 [0003]
Conventionally, the raw materials from each fixed hopper of iron ore and coke are supplied to the furnace turning chute via the storage hopper, and alternately charged and distributed in the furnace by tilting and turning of the furnace turning chute. A raw material charging method for a bell-less blast furnace is widely known. On the other hand, in order to maintain stable operation of the blast furnace, the ratio of iron ore and coke at each location in the furnace and the coke amount ratio and the layer state are kept constant, and the gas flow distribution in the furnace and the furnace heat distribution are maintained. It is important to make it uniform.
[0004]
Therefore, the present applicant has developed a raw material charging method for a blast furnace in which the level of the raw material inside the furnace is flattened and the particle size in the furnace radial direction is changed stepwise in the furnace radial direction. Previously proposed as Japanese Patent Publication No. 63-39642 (Japanese Patent Application No. 60-67396).
However, as a result of research conducted by the present inventors, it has been found that the dropping trajectory of the raw material falling from the storage hopper to the in-furnace swivel chute has a great influence on uniformizing the iron ore and coke layer state. That is, it has been found that when the raw material deposition level in the storage hopper fluctuates, the falling trajectory of the raw material changes, and a uniform raw material layer cannot be formed in the furnace. Accordingly, it has been desired to develop a new technique for keeping the raw material accumulation level in the storage hopper constant.
In addition, since the initial opening of the upper flow control gate has been set to a predetermined value obtained empirically, the material accumulation level in the storage hopper changes when the material accumulation changes due to changes in the particle size of the material, etc. There was also a problem that the controllability of the system was adversely affected.
[0005]
[Problems to be solved by the invention]
The present invention solves the conventional problems as described above, and by keeping the raw material accumulation level in the storage hopper below the fixed hopper constant, it is possible to stabilize the raw material falling trajectory, and further, the raw material It was completed for the purpose of providing a raw material charging method for a blast furnace that can charge the raw material while keeping the raw material deposition level constant without being affected by the next raw material charging even if the particle size changes. Is.
[0006]
[Means for Solving the Problems]
The raw material charging method of the blast furnace of the present invention made to solve the above problems is to supply the raw materials of each fixed hopper of iron ore and coke alternately to the in-furnace swivel chute via the storage hopper, In the blast furnace raw material charging method in which the turning chute is tilted and swirled into the furnace, the upper flow adjustment gate at the lower part of the fixed hopper is set for each upper flow adjustment gate in each fixed hopper. (10a), when the base opening of the (10b), respectively (θ a), (θ b ), and the correction angle respectively set for each fixed hopper (β a), (β b ), The opening of the upper flow adjustment gate is set to a −β a ) or (θ b −β b ) at a predetermined level, and the opening of the upper flow adjustment gate is set to when the return to a) or (θ b), has become a high level The opening of the upper flow regulating gate and a -2β a) or b -2β b), back to when it reaches a predetermined level a a) or b b) The average of the upper flow control gate is calculated using data obtained by converting and quantifying the level to which the accumulation of each material belongs in the total time in one raw material charging process. The opening is calculated, and based on this value, the initial opening of the upper flow adjustment gate of each fixed hopper at the time of the next raw material charging is determined.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
In Figure 1, 1 a are each fixed hopper of iron ore, 1b coke fixed hopper, 2 a blast furnace body, said the stationary hopper iron ore and coke are charged interchanged at a constant period. These raw materials are charged into the fixed hoppers 1 a and 1 b through the belt conveyor 3 and the switching chute 4 at the top. The iron ore and the coke raw material stored in the fixed hoppers 1 a and 1 b are alternately supplied to the in-furnace turning chute 6 through the storage hopper 5, and the in-furnace turning chute 6 is tilted and swung in the furnace. The above raw material charging process is basically the same as the conventional bellless type blast furnace raw material charging method.
[0008]
In the present invention, the amount of the raw material is adjusted while adjusting the degree of opening of the upper flow control gate 10 at the lower portion of the fixed hopper so that the amount of the raw material is kept constant based on the level meter 7 installed in the storage hopper 5. At the same time, the average opening degree of the upper flow adjustment gate 10 at this time is calculated, and the initial opening degree of the upper flow adjustment gate 10 at the next raw material charging is determined based on this value. It has characteristics.
[0009]
More specifically, a level meter 7 for measuring the amount of raw material accumulated is installed in the storage hopper 5. Specifically, three level meters 7, 7, and 7 (from the top to H, M, and L) are installed in the vertical direction, and signals from each level meter when material accumulates beyond the level meter. Of the total time in one raw material charging process, it is determined whether the raw material accumulation level belongs to any of the four levels of less than level L, level L to M, level M to H, or level H or higher. It is configured to convert and quantify.
[0010]
Then, based on the numerical value quantified as described above, the opening degree of the upper flow adjustment gate 10 is adjusted, and fine adjustment is performed so that the accumulation state of the raw material is maintained in the vicinity of the level M.
That is, each upper flow regulating gate 10 a, 10 b of the base opening degree, respectively (θ a), (θ b ) and when, the upper flow regulating gate 10 a as they become level M, 10 b of the opening Is a −β a ) or (θ b −β b ) . Here, β a and β b are correction angles set for the iron ore, the coke brand, and each fixed hopper. Then, returning the opening degree of the upper flow regulating gate 10 a, 10 b when it becomes level L in (theta a) or (θ b). Further, when the level H is reached, the opening degree of each upper flow control gate 10 a , 10 b is set to a -2β a ) or (θ b -2β b ), and when the level M is reached a Adjustment is made so as to return to −β a or (θ b −2β b ) .
Note that the levels M and H are detected, and the opening of the upper flow adjustment gate 10 is set to a −β a ), (θ b −β b ), (θ a −2β a ), or (θ b −2β b ) . If the level does not return to L or M even after a lapse of a certain time, the opening degree of the upper flow adjustment gate 10 is returned to the base opening degree (θ) as an input value abnormality and is controlled again.
[0011]
In addition, the average opening of the upper flow adjustment gate is obtained by using the data obtained by converting and quantifying the level of the raw material accumulation level in the total time in one raw material charging process. Based on this value, the initial opening degree of the upper flow adjustment gate at the time of the next raw material charging is determined. As a result, even if there is a change in the amount of accumulation due to a change in the raw material particle size, etc., the initial opening of the upper flow control gate is an appropriate value, so there will be no adverse effects when the raw material is charged the next time, and smooth It is possible to carry out a raw material charging.
In addition, the determination of the initial opening of the upper flow adjustment gate at the time of the next raw material charging is, specifically, in the total time in one raw material charging process, the amount of raw material accumulation is less than level L, level L ~ Calculate the time ratio of each level based on the value obtained by converting the time of M, level M to H, or higher level H or higher to level H and converting it to time (calculated as the ratio when the total is 100) The average value obtained by multiplying this by the correction coefficient is taken as the average level. Then, the initial level of the upper flow adjustment gate is determined by adding a correction by ± in comparison with the average level.
[0012]
Thus, according to the present invention, the opening of the upper flow control gate 10 at the lower part of the fixed hopper is adjusted so that the amount of the material accumulated is constant based on the level meter 7 installed in the storage hopper 5. At the same time, the average opening of the upper flow adjustment gate 10 at this time was calculated, and the initial opening of the upper flow adjustment gate 10 at the time of the next raw material charging was determined based on this value. For example, even if there is a change in the particle size of the raw material, the raw material deposition level in the storage hopper is kept constant. As a result, since the raw material can always be dropped to the in-furnace swivel chute 6 under a certain condition, the ratio of the amount of iron ore and the amount of coke and the layer state at each position in the furnace are kept constant. A stable blast furnace operation can be secured with a constant reaction.
[0013]
【The invention's effect】
As is clear from the above description, the present invention can stabilize the material dropping trajectory by keeping the material accumulation level in the storage hopper below the fixed hopper constant, and further change the particle size of the material. Even if there is, etc., the raw material can be charged while keeping the raw material deposition level constant without being affected at the next raw material charging.
Therefore, the present invention greatly contributes to the development of industry as a raw material charging method for a blast furnace that eliminates conventional problems.
[Brief description of the drawings]
FIG. 1 is a front view showing an embodiment of the present invention.
[Explanation of symbols]
1 a iron ore fixed hopper
1 b Coke fixed hopper 2 Blast furnace body 5 Storage hopper 7 Level meter
10 a upper flow control gate
10 b upper flow regulating gate 11 lower flow regulating gate

Claims (1)

鉄鉱石およびコークスの各固定ホッパーの原料を貯留ホッパーを介して炉内旋回シュートに交互に供給し、該炉内旋回シュートの傾動および旋回により炉内に装入分配する高炉の原料装入方法において、前記固定ホッパー下部にある上部流調ゲートの開度を、各固定ホッパー毎に設定される各上部流調ゲート( 10a )、( 10b )のベース開度をそれぞれ(θ a )、(θ b )、および各固定ホッパー毎に設定される補正角度をそれぞれ(β a )、(β b とした場合に、所定のレベルになった時点で上部流調ゲートの開度を(θ a −β a )あるいは(θ b −β b とし、低いレベルになった時点で上部流調ゲートの開度を(θ a )あるいは(θ b に戻し、高いレベルになった時点で上部流調ゲートの開度を(θ a −2β a )あるいは(θ b −2β b とし、所定のレベルになった時点で(θ a −β a )あるいは(θ b −β b に戻すように調整して、1回の原料装入工程における全時間のうち、各原料の溜まり具合がいずれのレベルに属するかを時間に換算し定量化したデータを用いて、上部流調ゲートの平均開度を算出し、この値を基に次回の原料装入時における各固定ホッパーの上部流調ゲートの初期開度を決定することを特徴とする高炉の原料装入方法。In a raw material charging method for a blast furnace in which raw materials of each fixed hopper of iron ore and coke are alternately supplied to a swivel chute in a furnace through a storage hopper, and charged and distributed in the furnace by tilting and swiveling of the swivel chute in the furnace , The opening of the upper flow adjustment gate below the fixed hopper, and the base opening of each upper flow adjustment gate ( 10a ), ( 10b ) set for each fixed hopper , respectively (θ a ), (θ b ), And the correction angles set for each fixed hopper are (β a ) and (β b ) , respectively , the opening of the upper flow adjustment gate is a −β a ) or (θ b −β b ). When the level becomes low, the opening of the upper flow adjustment gate is returned to a ) or (θ b ) , and when it becomes a high level, the upper flow adjustment gate the opening and a -2β a) or b -2β b) Adjusts back to a a) or b b) when it becomes a predetermined level, of the total time in one raw material charging step, reservoir of each raw material condition The average opening of the upper flow control gate is calculated using data that is converted to time and quantified to which level belongs, and based on this value, the upper flow of each fixed hopper at the next raw material charging is calculated. A raw material charging method for a blast furnace, characterized by determining an initial opening of the adjusting gate.
JP2002272584A 2002-09-19 2002-09-19 Raw material charging method for blast furnace Expired - Lifetime JP3978105B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002272584A JP3978105B2 (en) 2002-09-19 2002-09-19 Raw material charging method for blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002272584A JP3978105B2 (en) 2002-09-19 2002-09-19 Raw material charging method for blast furnace

Publications (2)

Publication Number Publication Date
JP2004107732A JP2004107732A (en) 2004-04-08
JP3978105B2 true JP3978105B2 (en) 2007-09-19

Family

ID=32269567

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002272584A Expired - Lifetime JP3978105B2 (en) 2002-09-19 2002-09-19 Raw material charging method for blast furnace

Country Status (1)

Country Link
JP (1) JP3978105B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101497571B1 (en) * 2014-06-17 2015-03-02 주식회사 한국테크놀로지 Apparatus for Supply Coal for Dust-Reduction and Dispersion Supply in System for Drying Coal

Also Published As

Publication number Publication date
JP2004107732A (en) 2004-04-08

Similar Documents

Publication Publication Date Title
JP3978105B2 (en) Raw material charging method for blast furnace
JP2000178616A (en) Method for charging iron ore having high blending ratio pellet into blast furnace
JP3787240B2 (en) How to charge the blast furnace center
JP3787238B2 (en) Charging method into the center of the blast furnace
JPS61223113A (en) Raw material charging method for blast furnace
JP3787239B2 (en) Charging method into the center of the blast furnace
JP3787231B2 (en) How to charge the blast furnace center
JP3787236B2 (en) How to charge the blast furnace center
JPH0225507A (en) Method and apparatus for charging raw material in bell-less type blast furnace
JP2001049312A (en) Method for charging raw material in bell-less blast furnace
JPS62224608A (en) Operating method for bell-less type blast furnace
JP2000178617A (en) Method for charging charging material for activating furnace core part in blast furnace
JP3750148B2 (en) Raw material charging method and apparatus for blast furnace
JP2847994B2 (en) Raw material charging method for bellless blast furnace
UA147951U (en) METHOD OF LOADING MACHINE MATERIALS INTO THE DOMAIN FURNACE
JPS62260009A (en) Charging method for pellet-compounded raw material in bell-less type blast furnace
JPH11217605A (en) Method for charging charging material into blast furnace
JP2001262207A (en) Raw material charging method in blast furnace
JP2001140009A (en) Method of charging raw material into blast furnace
JP2004204322A (en) Method for charging raw material for blast furnace
JP3702008B2 (en) Blast furnace operation method
JP2022157588A (en) Blast furnace operation method, blast furnace operation control device, and blast furnace operation control program
JPH09241711A (en) Method for estimating crumbling quantity of coke and preventing method thereof
JP2000273508A (en) Method for strengthening center gas flow in blast furnace
JPS6314808A (en) Raw material charging method for bell-less type blast furnace

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040901

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20060119

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060124

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060327

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070327

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070524

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070615

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070622

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100629

Year of fee payment: 3

R151 Written notification of patent or utility model registration

Ref document number: 3978105

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100629

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110629

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110629

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120629

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130629

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130629

Year of fee payment: 6

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130629

Year of fee payment: 6

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130629

Year of fee payment: 6

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term