JPH06179904A - Pressure equalizing method in charging device for bell type blast furnace - Google Patents

Pressure equalizing method in charging device for bell type blast furnace

Info

Publication number
JPH06179904A
JPH06179904A JP35373392A JP35373392A JPH06179904A JP H06179904 A JPH06179904 A JP H06179904A JP 35373392 A JP35373392 A JP 35373392A JP 35373392 A JP35373392 A JP 35373392A JP H06179904 A JPH06179904 A JP H06179904A
Authority
JP
Japan
Prior art keywords
small bell
hopper
bell hopper
pressure
small
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.)
Granted
Application number
JP35373392A
Other languages
Japanese (ja)
Other versions
JP2785093B2 (en
Inventor
Yoshifusa Sato
良房 佐藤
Norihiko Kaneda
法彦 金田
Toshio Ono
敏雄 小野
Yoshikatsu Goto
吉克 後藤
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 JP4353733A priority Critical patent/JP2785093B2/en
Publication of JPH06179904A publication Critical patent/JPH06179904A/en
Application granted granted Critical
Publication of JP2785093B2 publication Critical patent/JP2785093B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To reduce a production cost in a blast furnace operation by stopping the introduction of inert gas into a small bell hopper, in the case of charging raw material in the small bell hopper into a large bell hopper. CONSTITUTION:Clean blast furnace gas is introduced into the small bell hopper 3 in the condition of closing the small bell 6 incorporating the raw material to execute a primary pressure equalization. By introducing the inert gas into the small bell hopper 3 based on the differential pressure between the small bell hopper 3 and the large bell hopper 4 till charging the following raw material into the small bell hopper 3, a secondary pressure equalization is executed so as to keep the pressures in both hoppers 3, 4 to almost the same. Then, by opening the small bell 6 during the secondary pressure equalization, the raw material in the small bell hopper 3 is charged into the large bell hopper 4. In this case, the introduction of the inert gas in the small bell hopper 3 is stopped. By this method, waste consumption of the nitrogen gas which does not directly affect the pressure equalization in the secondary pressure equalization process can be eliminated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ベル式高炉の炉頂から
炉内部へ原料を装入する際に行う原料装入装置の均圧方
法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure equalizing method for a raw material charging device when charging a raw material from the top of a bell type blast furnace to the inside of the furnace.

【0002】[0002]

【従来の技術】高炉の高圧操業においては、ベル及びシ
ール弁の開閉のため大ベルホッパー内及び小ベルホッパ
ー内の均圧及び排圧が必要である。例えば、小ベルホッ
パーと大ベルホッパーとからなる原料装入装置では、小
ベルホッパー内に原料を装入し、小ベルが閉状態から小
ベルホッパー上部に設けたシール弁開放前までの間は炉
頂圧力とほぼ同一の圧力で均圧し、この均圧が終わった
時点からシール弁開放直前までの間は小ベルホッパー内
の圧力を排圧してほぼ大気圧としている。この均圧は清
浄高炉ガスを用いて粗均圧を行う一次均圧と、不活性ガ
スとしての窒素ガスを用いて一次均圧で不足した圧力補
充と微調整均圧を行う二次均圧よりなっている。
2. Description of the Related Art In high-pressure operation of a blast furnace, pressure equalization and exhaust pressure in the large bell hopper and the small bell hopper are required to open and close the bell and the seal valve. For example, in a raw material charging device composed of a small bell hopper and a large bell hopper, the raw material is charged into the small bell hopper, and from the closed state of the small bell to the opening of the seal valve provided at the upper part of the small bell hopper. The pressure is almost equalized to the pressure at the furnace top, and the pressure in the small bell hopper is discharged to almost atmospheric pressure from the time when this pressure equalization ends to the time immediately before the opening of the seal valve. This pressure equalization is based on the primary pressure equalization that performs coarse pressure equalization using clean blast furnace gas and the secondary pressure equalization that performs insufficient pressure supplementation and fine adjustment pressure equalization using nitrogen gas as an inert gas. Has become.

【0003】従来の二次均圧方法における各装置の動作
を示すタイムチャートを図3に示す。二次均圧において
は、原料の装入タイムスケジュールにしたがって、二次
均圧開始から停止指令が出されるまでの間、つまり、一
次均圧が完了した後から、前記排圧を開始するまでの
間、小ベルホッパーと大ベルホッパー間の差圧が常に
「0」に近似するよう、窒素ガスを小ベルホッパー内に
導入している。すなわち、二次均圧開始指令が出される
と圧力調節計がオンとなり、圧力調節計の出力に基づき
調節弁が作動し、窒素ガスが小ベルホッパー内に流入し
て均圧が行われる。
FIG. 3 is a time chart showing the operation of each device in the conventional secondary pressure equalizing method. In the secondary pressure equalization, according to the raw material charging time schedule, from the start of the secondary pressure equalization until the stop command is issued, that is, after the completion of the primary pressure equalization until the discharge pressure is started. Meanwhile, nitrogen gas is introduced into the small bell hopper so that the pressure difference between the small bell hopper and the large bell hopper is always close to "0". That is, when the secondary pressure equalization start command is issued, the pressure regulator is turned on, the control valve operates based on the output of the pressure regulator, and nitrogen gas flows into the small bell hopper to perform pressure equalization.

【0004】そして、二次均圧を行っている最中に、小
ベルホッパー内に装入された原料を大ベルホッパー内に
装入するために小ベルを開くと、原料の落下に伴い瞬間
的に小ベルホッパー内の圧力が大ベルホッパー内の圧力
より低くなる。そこで、圧力調節計の出力に基づき、再
び調節弁が作動し窒素ガスが小ベルホッパー内に流入し
て均圧が行われる。この場合、小ベルホッパーと大ベル
ホッパーとの差圧を解消するため、大量の窒素ガスが小
ベルホッパー内に流入する。
When the small bell is opened to load the raw material charged in the small bell hopper into the large bell hopper during the secondary pressure equalization, the moment when the raw material falls, Therefore, the pressure in the small bell hopper becomes lower than the pressure in the large bell hopper. Then, based on the output of the pressure regulator, the regulating valve is actuated again and nitrogen gas flows into the small bell hopper to equalize the pressure. In this case, a large amount of nitrogen gas flows into the small bell hopper in order to eliminate the pressure difference between the small bell hopper and the large bell hopper.

【0005】[0005]

【発明が解決しようとする課題】しかし、小ベルホッパ
ーから大ベルホッパーへ原料が落下、移動したために発
生する両ホッパー間の差圧は、前記のように瞬間的なも
のであり、時間の経過に伴って解消されるにもかかわら
ず、窒素ガスを導入している。
However, the pressure difference between the two hoppers caused by the dropping and moving of the raw material from the small bell hopper to the large bell hopper is instantaneous as described above, and the passage of time. Nitrogen gas is being introduced even though it has been resolved due to.

【0006】この窒素ガスの導入量は、二次均圧で使用
する全窒素ガス量の約45%にもなり、不必要な窒素ガ
スの使用は生産コストの上昇を招くことになる。したが
って、二次均圧における窒素ガス使用量の無駄を省くた
め、均圧制御方法の適正化が望まれている。
The amount of nitrogen gas introduced is about 45% of the total amount of nitrogen gas used for secondary pressure equalization, and the unnecessary use of nitrogen gas leads to an increase in production cost. Therefore, in order to avoid waste of the nitrogen gas usage amount in the secondary pressure equalization, it is desired to optimize the pressure equalization control method.

【0007】[0007]

【課題を解決するための手段】本発明は、上記に鑑み提
案されたもので、原料を収容して小ベルが閉状態の小ベ
ルホッパーに清浄高炉ガスを導入して一次均圧を行い、
その後から次の原料を小ベルホッパー内に装入するまで
の間、小ベルホッパーと大ベルホッパー間の圧力差に基
づき、不活性ガスを小ベルホッパー内に導入して小ベル
ホッパー内の圧力と大ベルホッパー内の圧力をほぼ同一
に維持するように二次均圧行うベル式高炉の装入装置に
おける均圧方法において、上記二次均圧中に、小ベルを
開にして小ベルホッパー内の原料を大ベルホッパーへ装
入する場合に、小ベルホッパー内への不活性ガスの導入
を停止することを特徴とする。
The present invention has been proposed in view of the above, and introduces a clean blast furnace gas into a small bell hopper containing a raw material and having a small bell closed to perform primary pressure equalization,
After that, until the next raw material is charged into the small bell hopper, the inert gas is introduced into the small bell hopper based on the pressure difference between the small bell hopper and the large bell hopper, and the pressure in the small bell hopper is introduced. And a method for equalizing the pressure in a bell-type blast furnace that performs secondary pressure equalization so as to maintain the pressure in the large bell hopper substantially the same, the small bell hopper is opened by opening the small bell during the secondary pressure equalization. When charging the raw materials in the large bell hopper, the introduction of the inert gas into the small bell hopper is stopped.

【0008】[0008]

【作用】本発明の均圧方法によれば、高炉ガスにより一
次均圧を行った後、二次均圧開始指令により不活性ガス
である窒素ガスを小ベルホッパー内に導入して、小ベル
ホッパーと大ベルホッパーの圧力差がほぼ「0」となる
よう二次均圧を行う。ここで、小ベルホッパー内に装入
した原料を大ベルホッパーへ装入するため小ベルを開く
必要がある。この際、小ベルホッパーと大ベルホッパー
間に原料の落下による圧力差が生じる。この場合、両ホ
ッパー間の圧力差は長く続くものではなく、しかも原料
装入に支障をきたすものではない。また、小ベルを開い
た状態で窒素ガスを流入させたとしても、窒素ガスは小
ベルホッパー及び大ベルホッパーの両方へ流入するの
で、均圧への利目が小さいため、窒素ガスが小ベルホッ
パー内に流入しないようにする。したがって、二次均圧
工程において均圧に直接影響を与えない無駄な窒素ガス
を消費することがなく、製造コストを低減することが可
能となる。
According to the pressure equalizing method of the present invention, after the primary pressure equalization is performed by the blast furnace gas, the nitrogen gas which is an inert gas is introduced into the small bell hopper by the secondary pressure equalization start command, Secondary equalization is performed so that the pressure difference between the hopper and the large bell hopper becomes almost "0". Here, it is necessary to open the small bell in order to charge the raw material charged in the small bell hopper into the large bell hopper. At this time, a pressure difference occurs between the small bell hopper and the large bell hopper due to the dropping of the raw material. In this case, the pressure difference between the two hoppers does not last long and does not hinder the charging of the raw materials. Even if nitrogen gas is introduced with the small bell open, the nitrogen gas flows into both the small bell hopper and the large bell hopper, so there is little advantage in equalizing the pressure, so the nitrogen gas is small. Do not let it flow into the hopper. Therefore, it is possible to reduce the manufacturing cost without consuming unnecessary nitrogen gas that does not directly affect the pressure equalization in the secondary pressure equalization step.

【0009】[0009]

【実施例】以下、図面に基づいて本発明の一実施例を説
明する。図1は、本発明に係る高炉1の模式図である。
高炉1は、炉頂部に原料ホッパー2を有し、原料ホッパ
ー2の下部に小ベルホッパー3を設け、小ベルホッパー
3の下部に大ベルホッパー4を設けてある。原料ホッパ
ー2と小ベルホッパー2との間にはシール弁5が設けて
あり、原料ホッパー2と小ベルホッパー3とを隔離す
る。また、小ベルホッパー3と大ベルホッパー4との間
には小ベル6が昇降可能に設けてあり、小ベル6が小ベ
ルホッパー3の下面に圧接することにより小ベルホッパ
ー3と大ベルホッパー4とを隔離する。さらに、大ベル
ホッパー4と炉内部7との間には大ベル8が昇降可能に
設けてあり、大ベル8が大ベルホッパー4の下面に圧接
することにより大ベルホッパー4と炉内部7とを隔離す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram of a blast furnace 1 according to the present invention.
The blast furnace 1 has a raw material hopper 2 at the top of the furnace, a small bell hopper 3 is provided below the raw material hopper 2, and a large bell hopper 4 is provided below the small bell hopper 3. A seal valve 5 is provided between the raw material hopper 2 and the small bell hopper 2 to separate the raw material hopper 2 and the small bell hopper 3 from each other. Further, a small bell 6 is provided between the small bell hopper 3 and the large bell hopper 4 so as to be able to move up and down. Isolate 4 and. Further, a large bell 8 is provided between the large bell hopper 4 and the inside of the furnace 7 so as to be able to move up and down, and when the large bell 8 is pressed against the lower surface of the large bell hopper 4, the large bell hopper 4 and the inside of the furnace 7 are connected. Isolate.

【0010】小ベルホッパー3及び大ベルホッパー4に
は、それぞれ圧力配管9a,9bを介して差圧計10が
連絡している。そして、この差圧計10からの出力は、
調節計11に入力している。また、小ベルホッパー3に
は開閉弁12及び調節弁13を介して窒素ガス供給設備
14が接続してあり、均圧に使用する窒素ガスを供給し
ている。上記した調節計11は、差圧計10からの出力
に基づき調節弁13を作動させるための装置で、制御手
段である均排圧シーケンサ15からの二次均圧開始指令
に基づいて能動化し、調節弁13に作動信号を送信す
る。
A differential pressure gauge 10 is connected to the small bell hopper 3 and the large bell hopper 4 via pressure pipes 9a and 9b, respectively. And the output from this differential pressure gauge 10 is
It is input to the controller 11. Further, a nitrogen gas supply facility 14 is connected to the small bell hopper 3 via an opening / closing valve 12 and a control valve 13 to supply nitrogen gas used for pressure equalization. The above-mentioned controller 11 is a device for operating the control valve 13 based on the output from the differential pressure gauge 10, and is activated and adjusted based on the secondary pressure equalization start command from the pressure equalization sequencer 15 which is the control means. An actuation signal is sent to the valve 13.

【0011】また、小ベル開閉用シャフト6aには小ベ
ル6の開閉を検知する開閉検知スイッチ16が連絡して
あり、小ベル6が開くと小ベル開信号を均排圧シーケン
サ15に出力する。この小ベル開信号を受信した均排圧
シーケンサ15は、調節計11に対して出力していた二
次均圧開始指令信号を停止して差圧計10を非能動化
し、二次均圧開始指令が出されている間であっても調節
弁13への作動信号の送信を抑制する。
Further, an opening / closing detection switch 16 for detecting the opening / closing of the small bell 6 is connected to the small bell opening / closing shaft 6a, and when the small bell 6 is opened, a small bell opening signal is output to the uniform discharge pressure sequencer 15. . Upon receiving the small bell open signal, the pressure equalizing pressure sequencer 15 deactivates the differential pressure gauge 10 by stopping the secondary pressure equalization start command signal output to the controller 11, and the secondary pressure equalization start command is issued. The transmission of the actuation signal to the control valve 13 is suppressed even while is being issued.

【0012】上記した均排圧シーケンサ15における制
御動作を図2に示したフローチャートに基づき説明す
る。二次均圧を行うための二次均圧開始指令が出力され
ると、監視タイマーを作動させ、小ベル6の開閉動作を
判断する。そして、開閉検知スイッチ16が小ベル6の
開状態を検知すると監視タイマーの状態を調べ、監視タ
イマーがタイムアップしていると、調節弁13を全閉状
態とし小ベルホッパー3への窒素ガスの供給を停止す
る。ここで、監視タイマーの状態を調べているのは、何
らかの原因で小ベル6が微動し、開閉スイッチ16が開
状態を検知した場合にまで、調節弁13を全閉状態とす
ることを防ぐためである。すなわち、実際に小ベルホッ
パー3内の原料を大ベルホッパー4内に装入するため
に、小ベル6が開状態となった場合にのみ調節弁13を
全閉状態とする。
The control operation of the above-mentioned pressure equalization sequencer 15 will be described with reference to the flow chart shown in FIG. When the secondary pressure equalization start command for performing the secondary pressure equalization is output, the monitoring timer is activated to judge the opening / closing operation of the small bell 6. When the open / close detection switch 16 detects the open state of the small bell 6, the state of the monitoring timer is checked, and when the monitoring timer is up, the control valve 13 is fully closed and nitrogen gas is supplied to the small bell hopper 3. Stop the supply. Here, the state of the monitoring timer is checked to prevent the control valve 13 from being fully closed until the small bell 6 slightly moves for some reason and the open / close switch 16 detects the open state. Is. That is, in order to actually load the raw material in the small bell hopper 3 into the large bell hopper 4, the control valve 13 is fully closed only when the small bell 6 is opened.

【0013】一方、小ベル6が閉状態である場合、及び
監視タイマーがタイムアップしていない場合には、自動
制御により調節弁を制御し、小ベルホッパー3内に流入
する窒素ガス量を調節して均圧を行う。また、二次均圧
開始指令の出力が停止すると、調節弁13を全閉状態と
して小ベルホッパー3への窒素ガスの供給を停止し、二
次均圧を終了する。
On the other hand, when the small bell 6 is in the closed state and when the monitoring timer has not timed out, the control valve is automatically controlled to control the amount of nitrogen gas flowing into the small bell hopper 3. And equalize. When the output of the secondary pressure equalization start command is stopped, the control valve 13 is fully closed to stop the supply of nitrogen gas to the small bell hopper 3, and the secondary pressure equalization is ended.

【0014】[0014]

【発明の効果】以上説明したように、本発明では、高炉
炉頂から高炉内部へ原料を装入する際に行う均圧工程に
おいて、高炉ガスを小ベルホッパーに導入して一次均圧
を行った後、二次均圧開始指令が出されると、小ベルホ
ッパーと大ベルホッパー間の圧力差を計測し、該計測値
に基づき、不活性ガスを小ベルホッパー内に導入して小
ベルホッパー内の圧力と大ベルホッパー内の圧力をほぼ
同一に維持するよう二次均圧制御を行い、上記二次均圧
制御中に、小ベルホッパー内に装入した原料を大ベルホ
ッパーへ装入するため小ベルを開いても、小ベルホッパ
ー内への不活性ガスの流入を停止している。
As described above, in the present invention, in the pressure equalizing step performed when charging the raw material from the blast furnace top to the inside of the blast furnace, the blast furnace gas is introduced into the small bell hopper to perform the primary pressure equalization. After that, when the secondary pressure equalization start command is issued, the pressure difference between the small bell hopper and the large bell hopper is measured, and based on the measured value, the inert gas is introduced into the small bell hopper and the small bell hopper is introduced. The secondary pressure equalization control is performed so that the internal pressure and the pressure in the large bell hopper are kept almost the same, and during the above secondary pressure equalization control, the raw material charged in the small bell hopper is charged into the large bell hopper. Therefore, even if the small bell is opened, the flow of the inert gas into the small bell hopper is stopped.

【0015】すなわち、小ベルホッパー内に装入した原
料を大ベルホッパーへ装入するため小ベルを開いた場合
に生じる小ベルホッパーと大ベルホッパー間の圧力差
は、原料装入に何等支障をきたさないため、このような
場合には窒素ガスが小ベルホッパー内へ流入しないよう
に制御している。したがって、二次均圧工程において均
圧に直接影響を与えない無駄な窒素ガスを消費すること
がなく、高炉操業における製造コストを低減することが
可能となる。
That is, the pressure difference between the small bell hopper and the large bell hopper, which occurs when the small bell is opened to load the raw material charged in the small bell hopper into the large bell hopper, does not hinder the charging of the raw material. Therefore, in such a case, the nitrogen gas is controlled so as not to flow into the small bell hopper. Therefore, it is possible to reduce the manufacturing cost in the blast furnace operation without consuming wasteful nitrogen gas that does not directly affect the pressure equalization in the secondary pressure equalization step.

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

【図1】本発明の一実施例を示す高炉の模式図である。FIG. 1 is a schematic view of a blast furnace showing an embodiment of the present invention.

【図2】均圧の制御手段である均排圧シーケンサにおけ
る制御動作を示したフローチャートである。
FIG. 2 is a flowchart showing a control operation in a pressure-equalizing pressure sequencer which is a pressure equalizing control means.

【図3】従来の均圧方法における各装置の動作を示すタ
イムチャートである。
FIG. 3 is a time chart showing the operation of each device in the conventional pressure equalizing method.

【符号の説明】[Explanation of symbols]

1 高炉 2 原料ホッパー 3 小ベルホッパー 4 大ベルホッパー 5 シール弁 6 小ベル 7 炉内部 8 大ベル 9a,9b 圧力配管 10 差圧計 11 調節計 12 開閉弁 13 調節弁 14 窒素ガス供給設備 15 均排圧シーケンサ 16 開閉検知スイッチ 1 Blast furnace 2 Raw material hopper 3 Small bell hopper 4 Large bell hopper 5 Seal valve 6 Small bell 7 Inside the furnace 8 Large bell 9a, 9b Pressure piping 10 Differential pressure gauge 11 Controller 12 Open / close valve 13 Control valve 14 Nitrogen gas supply equipment 15 Uniform discharge Pressure sequencer 16 Open / close detection switch

───────────────────────────────────────────────────── フロントページの続き (72)発明者 後藤 吉克 大分県大分市大字西ノ洲1番地 新日本製 鐵株式会社大分製鐵所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshikatsu Goto 1 Nishinosu, Oita-shi, Oita New Nippon Steel Co., Ltd. Oita Works

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】原料を収容して小ベルが閉状態の小ベルホ
ッパーに清浄高炉ガスを導入して一次均圧を行い、その
後から次の原料を小ベルホッパー内に装入するまでの
間、小ベルホッパーと大ベルホッパー間の圧力差に基づ
き、不活性ガスを小ベルホッパー内に導入して小ベルホ
ッパー内の圧力と大ベルホッパー内の圧力をほぼ同一に
維持するように二次均圧行うベル式高炉の装入装置にお
ける均圧方法において、上記二次均圧中に、小ベルを開
にして小ベルホッパー内の原料を大ベルホッパーへ装入
する場合に、小ベルホッパー内への不活性ガスの導入を
停止することを特徴としたベル式高炉の装入装置におけ
る均圧方法。
1. A clean bell hopper gas is introduced into a small bell hopper in which a small bell is closed and a small bell is closed to perform primary pressure equalization, and thereafter, the next raw material is charged into the small bell hopper. Based on the pressure difference between the small bell hopper and the large bell hopper, an inert gas is introduced into the small bell hopper so that the pressure inside the small bell hopper and the pressure inside the large bell hopper are kept almost the same. In a pressure equalizing method in a charging device of a bell-type blast furnace for performing pressure equalization, when the raw material in the small bell hopper is charged into the large bell hopper by opening the small bell during the secondary pressure equalization, the small bell hopper is used. A method for equalizing pressure in a bell-type blast furnace charging device characterized by stopping the introduction of an inert gas into the interior.
JP4353733A 1992-12-15 1992-12-15 Pressure equalization method in bell blast furnace charging equipment Expired - Lifetime JP2785093B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4353733A JP2785093B2 (en) 1992-12-15 1992-12-15 Pressure equalization method in bell blast furnace charging equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4353733A JP2785093B2 (en) 1992-12-15 1992-12-15 Pressure equalization method in bell blast furnace charging equipment

Publications (2)

Publication Number Publication Date
JPH06179904A true JPH06179904A (en) 1994-06-28
JP2785093B2 JP2785093B2 (en) 1998-08-13

Family

ID=18432852

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4353733A Expired - Lifetime JP2785093B2 (en) 1992-12-15 1992-12-15 Pressure equalization method in bell blast furnace charging equipment

Country Status (1)

Country Link
JP (1) JP2785093B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102732657A (en) * 2012-07-17 2012-10-17 新兴铸管股份有限公司 Method for clearing away blocking of pressure-equalizing diffusion pipeline of blast furnace with double-bell type furnace top

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102586520B (en) * 2012-01-10 2013-09-25 中冶南方工程技术有限公司 Method for carrying out voltage-sharing bleeding on furnace top of blast furnace
CN102586518A (en) * 2012-01-10 2012-07-18 中冶南方工程技术有限公司 Method for carrying out voltage-sharing bleeding on furnace top of blast furnace by using nitrogen
CN103103304A (en) * 2013-01-18 2013-05-15 宁波钢铁有限公司 Device and method capable of realizing belt pressing washing

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56169712A (en) * 1980-06-03 1981-12-26 Kobe Steel Ltd Equalization of pressure of uniform-pressure chamber at top of blast furnace
JPS5779104A (en) * 1980-11-06 1982-05-18 Kobe Steel Ltd Pressure equalizing method of blast furnace top ressure equalizing chamber
JPS5825408A (en) * 1981-08-05 1983-02-15 Kobe Steel Ltd Pressure equalizing method for top pressure equalizing chamber of blast furnace

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56169712A (en) * 1980-06-03 1981-12-26 Kobe Steel Ltd Equalization of pressure of uniform-pressure chamber at top of blast furnace
JPS5779104A (en) * 1980-11-06 1982-05-18 Kobe Steel Ltd Pressure equalizing method of blast furnace top ressure equalizing chamber
JPS5825408A (en) * 1981-08-05 1983-02-15 Kobe Steel Ltd Pressure equalizing method for top pressure equalizing chamber of blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102732657A (en) * 2012-07-17 2012-10-17 新兴铸管股份有限公司 Method for clearing away blocking of pressure-equalizing diffusion pipeline of blast furnace with double-bell type furnace top

Also Published As

Publication number Publication date
JP2785093B2 (en) 1998-08-13

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