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JPH0377403B2 - - Google Patents
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JPH0377403B2 - - Google Patents

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Publication number
JPH0377403B2
JPH0377403B2 JP58226140A JP22614083A JPH0377403B2 JP H0377403 B2 JPH0377403 B2 JP H0377403B2 JP 58226140 A JP58226140 A JP 58226140A JP 22614083 A JP22614083 A JP 22614083A JP H0377403 B2 JPH0377403 B2 JP H0377403B2
Authority
JP
Japan
Prior art keywords
boiler
blowing
water
converter
water supply
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
JP58226140A
Other languages
Japanese (ja)
Other versions
JPS60120104A (en
Inventor
Masumi Nishikawa
Sumio Iwamoto
Hideki Azuma
Masao Matsui
Masahiro Matsuo
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
Nippon Kokan Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Jukogyo KK, Nippon Kokan Ltd filed Critical Kawasaki Jukogyo KK
Priority to JP22614083A priority Critical patent/JPS60120104A/en
Publication of JPS60120104A publication Critical patent/JPS60120104A/en
Publication of JPH0377403B2 publication Critical patent/JPH0377403B2/ja
Granted legal-status Critical Current

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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Description

【発明の詳細な説明】 本発明は、転炉操業の安全性と転炉ボイラの安
全性を向上させた転炉ボイラの給水制御方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water supply control method for a converter boiler that improves the safety of converter operation and the safety of the converter boiler.

先ず、転炉操業の概要を説明する。高炉で生産
された溶銑は、転炉内に投入(以下装入という)
される。次に溶銑を装入した転炉内に純酸素を吹
き込み(以下吹錬という)、溶銑中に含まれる炭
素を除去し(以下精錬という)鋼を作る。この吹
錬中には、高温で且つ大量のCOガスが発生する。
精錬終了後、転炉内の溶鋼を取り出し(以下出鋼
という)、次の工程へと移る。
First, an overview of converter operation will be explained. The hot metal produced in the blast furnace is charged into the converter (hereinafter referred to as charging).
be done. Next, pure oxygen is blown into the converter charged with hot metal (hereinafter referred to as blowing), and carbon contained in the hot metal is removed (hereinafter referred to as refining) to produce steel. During this blowing, high temperature and large amounts of CO gas are generated.
After refining, the molten steel in the converter is removed (hereinafter referred to as tapping) and the process moves on to the next step.

第1図は、転炉工場の概略を示すものであり、
吹錬中に転炉1から発生した大量の高温COガス
は、誘引送風機8によつてフード3内に誘引さ
れ、ボイラ5で冷却された後除塵機6,7で除塵
し、ガスホルダ10に回収される。
Figure 1 shows an outline of the converter factory.
A large amount of high-temperature CO gas generated from the converter 1 during blowing is drawn into the hood 3 by the induced blower 8, cooled by the boiler 5, removed by dust removers 6 and 7, and collected in the gas holder 10. be done.

又吹錬の初期と未期におけるCO濃度の低い排
ガスは、切換ダンパ11によつて、煙突9を通し
て塔頂で燃焼の上大気中に放散される。なお、4
は、純酸素を吹込むための酸素ランスである。こ
のように転炉操業は、装入、吹錬、出鋼の各工程
によつて1回の製鋼工程が終り、これがくり返し
行われる。
In addition, exhaust gas with a low CO concentration at the beginning and early stages of blowing is combusted at the top of the tower through the chimney 9 by the switching damper 11, and then released into the atmosphere. In addition, 4
is an oxygen lance for blowing pure oxygen. In this way, in the converter operation, one steelmaking process is completed by each process of charging, blowing, and tapping, and this process is repeated.

従つて、転炉からのCOガスの発生も吹錬毎に
間歇的に発生し、これに従つて転炉ボイラも間歇
的に運転されることになる。
Therefore, CO gas is generated from the converter intermittently during each blowing process, and accordingly, the converter boiler is also operated intermittently.

又このCOガスは、外部に漏出すると非常に危
険であり、逆に装置内に外気が侵入すると爆発の
危険があるので、転炉ボイラは勿論のこと、除塵
器その他の装置は、密閉に保つ必要がある。
Also, this CO gas is extremely dangerous if it leaks outside, and conversely, there is a risk of explosion if outside air enters the equipment, so keep the converter boiler, dust remover, and other equipment tightly sealed. There is a need.

上記転炉ボイラの概略を次に説明する。第2図
において、フード3及びボイラ5は、水冷壁によ
つて形成され、この水冷壁内には、ボイラ循環ポ
ンプ13によつて冷却水が供給される。
The outline of the above converter boiler will be explained below. In FIG. 2, the hood 3 and the boiler 5 are formed by a water-cooled wall, into which cooling water is supplied by a boiler circulation pump 13.

転炉1で発生した高温のCOガスは、フード3
及びボイラ5の水冷壁によつて冷却されると共
に、冷却水は、COガスの熱を吸収して蒸発し、
ボイラドラム12に溜められる。19は蒸気配管
である。
The high temperature CO gas generated in converter 1 is transferred to hood 3.
The cooling water absorbs the heat of the CO gas and evaporates.
It is stored in the boiler drum 12. 19 is a steam pipe.

このようにして、COガスの熱を吸収して蒸発
し、蒸気配管19によつてその蒸気は消費される
ので、ボイラドラム12の水位が低下する。これ
を補うために、脱気器給水ポンプ17より脱気器
16に給水し、配管20より供給される蒸気によ
つて昇温されて脱気され、この給水を、ボイラ給
水ポンプ14により、ボイラドラム12に導い
て、ボイラドラム12の水位を保ち、ボイラの運
転を行う。
In this way, the heat of the CO gas is absorbed and evaporated, and the steam is consumed by the steam pipe 19, so that the water level in the boiler drum 12 is lowered. In order to compensate for this, water is supplied to the deaerator 16 from the deaerator feed water pump 17, heated and deaerated by the steam supplied from the piping 20, and this water is fed to the boiler by the boiler feed water pump 14. The water is introduced into the drum 12, the water level in the boiler drum 12 is maintained, and the boiler is operated.

又転炉ボイラは、間歇的に運転されるので、ボ
イラ給水ポンプ14による送水も間歇的となり、
この制御は、回転数制御装置18によつて、モー
タ15の回転数を制御し、これによつて給水ポン
プ14の回転数を変え、間歇運転に対する給水制
御を行つている。
Furthermore, since the converter boiler is operated intermittently, the water supply by the boiler feed water pump 14 is also intermittently,
In this control, the rotation speed of the motor 15 is controlled by the rotation speed control device 18, thereby changing the rotation speed of the water supply pump 14, thereby performing water supply control for intermittent operation.

このボイラ給水制御において、従来は、第3図
に示す制御パターンによつて行われていた。第2
図を参照しながら説明すると、吹錬開始と共に、
転炉1からは、大量の高温COガスが発生し、フ
ード3及びボイラ5内を循環している冷却水は蒸
発し、ボイラドラム12の水位が低下する。
Conventionally, this boiler water supply control has been performed according to a control pattern shown in FIG. Second
To explain with reference to the diagram, as soon as blowing begins,
A large amount of high-temperature CO gas is generated from the converter 1, the cooling water circulating in the hood 3 and the boiler 5 evaporates, and the water level in the boiler drum 12 decreases.

この状態は、第3図において、吹錬開始後ある
一定時間後に現われ、この時、回転数制御装置1
8が100%作動し、これにならつてモータ負荷電
力が100%となつて、給水ポンプ14は定格運転
となり、この給水ポンプ14により、ボイラ給水
量もその量に見合つた(定格流量)量だけ給水さ
れ、ボイラドラム12の水位が保たれるようにな
つていた。
In FIG. 3, this state appears after a certain period of time after the start of blowing, and at this time, the rotation speed control device 1
8 operates at 100%, and accordingly, the motor load power becomes 100%, and the water supply pump 14 becomes rated operation, and the water supply amount to the boiler is also adjusted to the amount corresponding to the amount (rated flow rate). Water was supplied and the water level in the boiler drum 12 was maintained.

このように、従来は、吹錬を開始し、ボイラド
ラム12の水位が低下した時点で回転数制御装置
18が作動し、給水されるようになつていた。
In this way, conventionally, when blowing is started and the water level in the boiler drum 12 falls, the rotational speed control device 18 is activated to supply water.

然し乍ら、何らかの原因で、回転数制御装置1
8が故障し作動しなかつた場合は、すでに吹錬が
開始されているので、ボイラドラム12の水位が
低下し、そのままの状態で運転した場合は、つい
に冷却水が不足し、フード3やボイラ5を焼損す
ることは勿論のこと、COガスの冷却が行われず
に高温度のまま流れるので、下流側に位置する除
塵機6,7や誘引送風機8も焼損し、非常に危険
な状態に陥ることになる。
However, for some reason, the rotation speed control device 1
If 8 fails and does not operate, blowing has already started, so the water level in the boiler drum 12 will drop, and if the operation continues in this state, the cooling water will eventually run out and the hood 3 and boiler Not only will the CO gas burn out, but the dust removers 6 and 7 and the induced blower 8 located downstream will also burn out as the CO gas is not cooled and flows at a high temperature, resulting in an extremely dangerous situation. It turns out.

このような事態を回避するためには、吹錬を中
止する以外に手段はなく、精錬に悪影響を及ぼす
ことになる。
In order to avoid such a situation, there is no other way than to stop the blowing, which will have a negative effect on the refining.

従つて、従来の転炉ボイラの給水制御は、転炉
操業の安全性と転炉ボイラの安全性の面で大きな
問題をかかえていた。
Therefore, conventional water supply control for converter boilers has had major problems in terms of the safety of converter operation and the safety of converter boilers.

本発明は、上記従来の問題を解決し、転炉操業
の安全性と、転炉ボイラの安全性を向上させた転
炉ボイラの給水制御方法を提供せんとするもので
ある。
The present invention aims to solve the above conventional problems and provide a water supply control method for a converter boiler that improves the safety of converter operation and the safety of the converter boiler.

即ち、本発明は吹錬開始前に回転数制御装置を
作動し、モータ負荷電力を上げて給水ポンプを定
格回転数まで回転し、給水系の作動状態を確認し
た上で、吹錬を開始するようにしたものであり、
吹錬開始直前に給水ポンプ駆動電動機の負荷電力
を一定値になるまで上げて給水ポンプを定格回転
数で回転させ、その後吹錬を開始し、吹錬中は、
ボイラドラムの水位に合せて給水し、吹錬終了時
はボイラドラムの水位に合せて給水ポンプの回転
数と給水ポンプ駆動電動機の負荷電力を低下させ
るようにしたものである。
That is, in the present invention, before the start of blowing, the rotation speed control device is activated, the motor load power is increased, the water supply pump is rotated to the rated rotation speed, and the operation state of the water supply system is confirmed, and then blowing is started. It was made so that
Immediately before the start of blowing, the load power of the water pump drive motor is increased to a certain value, the water pump is rotated at the rated speed, and then blowing is started.
Water is supplied in accordance with the water level in the boiler drum, and at the end of blowing, the rotation speed of the water pump and the load power of the water pump driving motor are reduced in accordance with the water level in the boiler drum.

以下、本発明の一実施例について、第2図を参
照しながら詳細に説明する。第4図において、高
炉で生産した溶銑を転炉1内に装入し、T1秒後
で且つ吹錬開始前に回転数制御装置18を作動さ
せると同時にモータ負荷電力を上げ給水ポンプを
定格回転数まで回転し給水系の作動状態を確認後
吹錬が開始される。吹錬初期の数秒間は、COガ
スの量も少なく、従つてボイラドラム12の水位
も変動しない。次に吹錬最盛期に入つて、大量の
COガスが発生し、フード3及びボイラ5内の冷
却水が蒸発し、ドラム12内の水位が低下し始め
る。この時、所定水量の給水がボイラドラム12
内に供給され、水位が保たれる。従つて吹錬最盛
期では、ボイラ循環ポンプ13によつて冷却水が
循環され、蒸気配管19より持ち去られていく蒸
気分だけ、給水ポンプ14によりボイラドラム1
2に給水し、ボイラドラム12内の水位を一定に
保つて、転炉ボイラを安全運転する。
Hereinafter, one embodiment of the present invention will be described in detail with reference to FIG. In Fig. 4, hot metal produced in a blast furnace is charged into the converter 1, and after T 1 second and before the start of blowing, the rotation speed control device 18 is activated, and at the same time, the motor load power is increased and the feed water pump is rated. After rotating to the maximum rotation speed and checking the operating status of the water supply system, blowing begins. During the initial few seconds of blowing, the amount of CO gas is small, and therefore the water level in the boiler drum 12 does not fluctuate. Next, entering the peak of blowing, a large amount of
CO gas is generated, the cooling water in the hood 3 and boiler 5 evaporates, and the water level in the drum 12 begins to drop. At this time, a predetermined amount of water is supplied to the boiler drum 12.
Water is supplied within the tank and the water level is maintained. Therefore, at the peak of blowing, the boiler circulation pump 13 circulates cooling water, and the water feed pump 14 pumps the boiler drum 1 by the amount of steam that is removed from the steam pipe 19.
2 and keep the water level in the boiler drum 12 constant to safely operate the converter boiler.

次に吹錬終了後、転炉1から発生するCOガス
量は減少するが、フード3及びボイラ5内ですで
に蒸発している蒸気分だけ、ボイラドラム12に
給水する必要があり、その分吹錬終了後T2秒間
は、給水ポンプ14は作動し、ボイラドラム12
内に給水される。ボイラドラムの水位が正常にな
つた時点で、回転数制御装置18によりモータ1
5の回転数を下げ、モータ負荷電力も下がる。こ
れで1回の製鋼工程が終了する。
Next, after the blowing is finished, the amount of CO gas generated from the converter 1 decreases, but it is necessary to supply water to the boiler drum 12 by the amount of steam that has already evaporated in the hood 3 and boiler 5. The water supply pump 14 operates for T 2 seconds after the completion of blowing, and the boiler drum 12
water is supplied inside. When the water level in the boiler drum becomes normal, the rotation speed control device 18 controls the motor 1.
5 and the motor load power also decreases. This completes one steelmaking process.

非吹錬時は、回転数制御装置18により、モー
タ15は低速回転し、消費電力は節減される。
During non-blowing, the motor 15 is rotated at a low speed by the rotation speed control device 18, thereby reducing power consumption.

以上詳述した通り、本発明による転炉ボイラの
給水制御方法によれば、吹錬開始前に回転数制御
装置を100%まで作動し、モータ負荷電力を上げ、
ボイラ給水装置が確実に作動することを確認した
後で吹錬を開始するようにしたので、回転数制御
装置が何らかの原因で故障して作動しない場合
は、吹錬開始は行われず、従つて吹錬を途中で中
止することも、又転炉ボイラやその他の機器の焼
損事故も発生しない。かくして転炉操業の安全性
と転炉ボイラの安全性が大巾に向上するという優
れた効果を奏する。
As detailed above, according to the water supply control method for a converter boiler according to the present invention, the rotation speed control device is operated to 100% before the start of blowing, the motor load power is increased,
Since blowing is started after confirming that the boiler water supply system operates reliably, if the rotation speed control device malfunctions for some reason and does not operate, blowing will not start. There is no need to stop the refining process midway through, and there is no risk of burnout of the converter boiler or other equipment. In this way, the safety of the converter operation and the safety of the converter boiler are greatly improved, which is an excellent effect.

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

第1図は転炉工場の概要を示す図、第2図は転
炉ボイラを系統図、第3図は従来の給水方法にお
いて、回転数制御パターンとモータ負荷電力とボ
イラ給水量との間の関係を経時的に示した図、第
4図は本発明の一実施例であり、回転数制御パタ
ーンとモータ負荷電力とボイラ給水量との間の関
係を経時的に示した図である。 1……転炉、2……スカート、3……フード、
5……ボイラ、12……ボイラドラム、13……
ボイラ循環ポンプ、14……ボイラ給水ポンプ、
15……モータ(ボイラ給水ポンプ駆動電動機)、
16……脱気器、18……回転数制御装置。
Figure 1 shows an overview of a converter factory, Figure 2 is a system diagram of a converter boiler, and Figure 3 shows the relationship between the rotation speed control pattern, motor load power, and boiler water supply amount in the conventional water supply method. FIG. 4 is a diagram showing the relationship over time, which is an embodiment of the present invention, and is a diagram showing the relationship between the rotational speed control pattern, motor load power, and boiler water supply amount over time. 1... converter, 2... skirt, 3... hood,
5... Boiler, 12... Boiler drum, 13...
Boiler circulation pump, 14...Boiler water supply pump,
15...Motor (boiler feed water pump drive electric motor),
16... Deaerator, 18... Rotation speed control device.

Claims (1)

【特許請求の範囲】[Claims] 1 吹錬開始直前に給水ポンプ駆動電動機の負荷
電力を一定値になるまで上げて給水ポンプを定格
回転数で回転させ、その後吹錬を開始し、吹錬中
はボイラドラムの水位に合せて給水し、吹錬終了
時はボイラドラムの水位に合せて給水ポンプの回
転数と給水ポンプ駆動電動機の負荷電力を低下さ
せることを特徴とする転炉ボイラの給水制御方
法。
1 Immediately before the start of blowing, increase the load power of the feed water pump drive motor to a certain value and rotate the feed water pump at the rated speed, then start blowing, and during blowing, feed water according to the water level of the boiler drum. A water supply control method for a converter boiler, characterized in that, at the end of blowing, the rotation speed of the water supply pump and the load power of the water supply pump drive motor are reduced in accordance with the water level of the boiler drum.
JP22614083A 1983-11-30 1983-11-30 Method of controlling feedwater to converter boiler Granted JPS60120104A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22614083A JPS60120104A (en) 1983-11-30 1983-11-30 Method of controlling feedwater to converter boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22614083A JPS60120104A (en) 1983-11-30 1983-11-30 Method of controlling feedwater to converter boiler

Publications (2)

Publication Number Publication Date
JPS60120104A JPS60120104A (en) 1985-06-27
JPH0377403B2 true JPH0377403B2 (en) 1991-12-10

Family

ID=16840475

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22614083A Granted JPS60120104A (en) 1983-11-30 1983-11-30 Method of controlling feedwater to converter boiler

Country Status (1)

Country Link
JP (1) JPS60120104A (en)

Also Published As

Publication number Publication date
JPS60120104A (en) 1985-06-27

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