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JPH0660794B2 - Preheating method for raw materials using exhaust gas - Google Patents
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JPH0660794B2 - Preheating method for raw materials using exhaust gas - Google Patents

Preheating method for raw materials using exhaust gas

Info

Publication number
JPH0660794B2
JPH0660794B2 JP5459088A JP5459088A JPH0660794B2 JP H0660794 B2 JPH0660794 B2 JP H0660794B2 JP 5459088 A JP5459088 A JP 5459088A JP 5459088 A JP5459088 A JP 5459088A JP H0660794 B2 JPH0660794 B2 JP H0660794B2
Authority
JP
Japan
Prior art keywords
exhaust gas
bucket
preheating
raw material
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 - Fee Related
Application number
JP5459088A
Other languages
Japanese (ja)
Other versions
JPH01230988A (en
Inventor
和夫 田中
正義 佐野
治男 大黒
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 JP5459088A priority Critical patent/JPH0660794B2/en
Publication of JPH01230988A publication Critical patent/JPH01230988A/en
Publication of JPH0660794B2 publication Critical patent/JPH0660794B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、溶解又は精錬を行う電気炉(以下、これを単
に電気炉という)で発生する排ガスを利用して、金属ス
クラップ,石灰石,鉄鉱石等の固形原料を予熱する方法
に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention utilizes exhaust gas generated in an electric furnace for melting or refining (hereinafter, simply referred to as an electric furnace) to produce metal scrap, limestone, iron ore. The present invention relates to a method of preheating a solid raw material such as stone.

〔従来の技術〕[Conventional technology]

たとえば、金属スクラップ等の原料を、予熱された状態
で電気炉に装入するとき、溶解又は精錬に消費される電
力等のエネルギーが予熱分だけ節減される。そして、予
熱状態で原料を装入するため、冷材の装入に比較し炉況
を大きく乱すことがないため、安定した操業状態が得ら
れる。また、最近では、バケットで一次予熱した原料の
仕上げ予熱に溶解炉又は精錬炉を使用し、可能な限り高
い温度に原料を予熱することが検討されている。
For example, when a raw material such as metal scrap is charged into an electric furnace in a preheated state, energy such as electric power consumed for melting or refining is reduced by the preheating amount. Since the raw material is charged in the preheated state, the furnace condition is not significantly disturbed as compared with the charging of the cold material, so that a stable operation state can be obtained. In addition, recently, it has been considered to use a melting furnace or a refining furnace for finishing preheating of the raw material which is preheated in a bucket and preheat the raw material to a temperature as high as possible.

この原料予熱のため、従来から、熱源として電気炉で発
生する排ガスを利用する各種の方法が提案されている。
この排ガスを原料予熱に利用するとき、排熱の回収が有
効に行われる。また、排ガスに浮遊しているダストも、
排ガスが原料層を通過することによって、その原料層に
捕捉・除去される。しかしながら、電気炉で発生する排
ガスの流量及び温度は、一定したものではなく、これを
そのまま原料予熱炉に送り込むと、排ガスの流量や温度
及び原料の通気抵抗等の変動によって電気炉の炉内圧が
変動し、操業状態が不安定になる。
For this preheating of the raw materials, various methods have been conventionally proposed in which exhaust gas generated in an electric furnace is used as a heat source.
When this exhaust gas is used for preheating the raw material, the exhaust heat is effectively recovered. Also, the dust floating in the exhaust gas,
As the exhaust gas passes through the raw material layer, it is captured and removed by the raw material layer. However, the flow rate and temperature of the exhaust gas generated in the electric furnace are not constant, and if this is sent to the raw material preheating furnace as it is, the furnace pressure of the electric furnace will change due to fluctuations in the flow rate and temperature of the exhaust gas and the ventilation resistance of the raw material. It fluctuates and the operating condition becomes unstable.

そこで、多量の排ガスが電気炉で発生した場合に、その
一部のみを原料予熱に使用することにより、炉内圧を制
御し操業状態に悪影響を与えないようにする方法が開発
されている。
Therefore, when a large amount of exhaust gas is generated in the electric furnace, a method has been developed in which only a part of the exhaust gas is used for preheating the raw material to control the internal pressure of the furnace so as not to adversely affect the operating state.

たとえば、アーク溶解中の電気炉の排ガスのみによって
原料予熱するとき、特公昭58-10674号公報においては、
アーク炉から予熱炉を経て冷却器及び排気ファンに至る
排ガスダクトの途中に、前記予熱炉を迂回するバイパス
管を設け、前記予熱炉に送り込まれる排ガスの温度が設
定値を超えたとき、バイパス管を経て排ガスを冷却器に
流している。
For example, when preheating the raw material only by the exhaust gas of the electric furnace during arc melting, in Japanese Patent Publication No. 58-10674,
In the middle of the exhaust gas duct from the arc furnace through the preheating furnace to the cooler and the exhaust fan, a bypass pipe bypassing the preheating furnace is provided, and when the temperature of the exhaust gas sent to the preheating furnace exceeds a set value, the bypass pipe The exhaust gas is passed to the cooler via the.

また、特開昭57-33787号公報においては、電気炉から予
熱炉を経て冷却器及び排気ファンに至る排ガスダクトの
途中に流量調整弁を設け、この流量調整弁により電気炉
の炉内圧を一定に維持し、操業状態を安定化させる方法
が採られている。
Further, in JP-A-57-33787, a flow rate adjusting valve is provided in the middle of the exhaust gas duct from the electric furnace to the cooler and the exhaust fan via the preheating furnace, and the furnace pressure of the electric furnace is kept constant by this flow rate adjusting valve. The method of maintaining the operating condition and stabilizing the operating condition is adopted.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

特公昭58-10674号公報のように、電気炉からバイパス管
を介して冷却器に排ガスを直接送り込む場合、冷却器に
おける温度変化が大きくなり、排ガスの冷却に使用され
る水等の冷媒の流量を複雑に変化させることが必要とな
る。また、排ガスが保有する熱量を、効率良く原料の予
熱に回収することができない。更には、排ガスが原料層
を通過することによるフィルタ効果が得られず、冷却器
に送り込まれる排ガスに多量のダストが浮遊するため、
広範囲にわたって変化するダスト濃度に対して有効なバ
グフィルタ等の除塵設備が必要とされる。
When the exhaust gas is directly sent from the electric furnace to the cooler through the bypass pipe as in Japanese Patent Publication No. 58-10674, the temperature change in the cooler becomes large and the flow rate of the refrigerant such as water used for cooling the exhaust gas. Needs to be changed in a complicated manner. In addition, the amount of heat held by the exhaust gas cannot be efficiently recovered for preheating the raw material. Furthermore, since the filter effect due to the exhaust gas passing through the raw material layer cannot be obtained, a large amount of dust floats in the exhaust gas sent to the cooler,
There is a need for dust removal equipment such as a bag filter that is effective for dust concentrations that change over a wide range.

また、特開昭57-33787号公報のように、排ガスダクトの
途中に設けた流量調整弁により炉内圧を一定に維持する
方法では、電気炉を2基又はそれ以上配置する場合、予
熱炉に送り込む排ガスの流量及び温度の変動幅が大き
く、且つ排ガスが予熱炉の原料層を通過するときの通気
抵抗も変動し、更に予熱炉の出側における排ガスの温度
も変化するため排風ファンの昇圧能力も変動する。これ
らの変動要因によって、炉内圧の制御精度が低下する。
このため、電気炉の排ガス集塵状態が不安定となり、炉
内圧上昇に伴う炉内からの発塵に起因して建屋内の環境
が悪化し、また炉内圧低下に伴い炉内への浸入空気によ
って熱効率の低下が生じる。
Further, as in Japanese Patent Laid-Open No. 57-33787, in a method of maintaining a constant furnace pressure by a flow rate control valve provided in the middle of an exhaust gas duct, when two or more electric furnaces are arranged, a preheating furnace is used. The fluctuation range of the flow rate and temperature of the exhaust gas sent in is large, the ventilation resistance when the exhaust gas passes through the raw material layer of the preheating furnace also changes, and the temperature of the exhaust gas at the exit side of the preheating furnace also changes, so the pressure of the exhaust fan rises. Ability also fluctuates. Due to these fluctuation factors, the accuracy of controlling the furnace pressure is reduced.
For this reason, the exhaust gas dust collection state of the electric furnace becomes unstable, and the environment inside the building deteriorates due to the dust generation from the inside of the furnace due to the rise of the pressure inside the furnace, and the infiltration air into the furnace due to the decrease of the pressure inside the furnace. Causes a decrease in thermal efficiency.

そこで、本発明は、電気炉で発生する排ガスの全量を制
御された流量条件の下でバケットに送り込むことによっ
て、排ガスが保有する熱量を原料予熱用熱源として有効
に回収すると共に、安定した条件下でバケット予熱を行
うことを目的とする。
Therefore, the present invention, by sending the total amount of the exhaust gas generated in the electric furnace into the bucket under controlled flow rate conditions, effectively recover the heat amount of the exhaust gas as a heat source for raw material preheating, and under stable conditions. The purpose is to preheat the bucket.

〔課題を解決するための手段及び作用〕[Means and Actions for Solving the Problems]

本発明の予熱方法は、その目的を達成するために、バケ
ット内で一次予熱した固形原料を電気炉に投入して二次
予熱し、次いで予熱された原料を前記電気炉内で溶解又
は精錬する際、前記電気炉を2基又はそれ以上配置し、
その一部が二次予熱状態にあるとき残りの電気炉を溶解
又は精錬状態に置き、前記バケットに至るダクトを経由
して前記複数の電気炉で発生した排ガスを前記バケット
に導き、前記ダクト内における排ガスのバケット入側圧
力に基づいて、前記バケットの出側に接続された排気ダ
クトに設けられている排気ファンの回転数を制御するこ
とを特徴とする。
In order to achieve the object, the preheating method of the present invention introduces a solid raw material, which is preheated in a bucket, into an electric furnace for secondary preheating, and then melts or refines the preheated raw material in the electric furnace. At this time, two or more electric furnaces are arranged,
When a part of it is in the secondary preheating state, the rest of the electric furnace is placed in a melting or refining state, the exhaust gas generated in the plurality of electric furnaces is guided to the bucket via a duct leading to the bucket, and inside the duct. Based on the inlet pressure of the exhaust gas in the bucket, the number of revolutions of the exhaust fan provided in the exhaust duct connected to the outlet side of the bucket is controlled.

以下、図面を参照しながら、本発明の特徴を具体的に説
明する。なお、以下の例においては、予熱される原料と
してステレンス鋼スクラップを使用したが、他の金属ス
クラップ,鉄鉱石,各種合金,石灰石等に対しても本発
明が同様に適用されるものであることは勿論である。
Hereinafter, the features of the present invention will be specifically described with reference to the drawings. In the following examples, stainless steel scrap was used as the raw material to be preheated, but the present invention is also applicable to other metal scraps, iron ores, various alloys, limestone, etc. Of course.

第1図は、本発明に従った原料予熱を説明するための全
体的なフローを示す。図示の場合、2基の電気炉を配置
し、これらを交互に仕上げ予熱及び溶解に使用してい
る。
FIG. 1 shows an overall flow for explaining the raw material preheating according to the present invention. In the illustrated case, two electric furnaces are arranged and are alternately used for finishing preheating and melting.

ステンレス鋼スクラップ等は、予熱原料1として先ずバ
ケット2に投入され、200〜300゜Cの温度に一次予熱され
る。次いで、予熱原料1は、電気炉3に装入される。こ
の電気炉3は、燃料の燃焼によって予熱原料1を加熱す
る加熱器4を備えている。予熱原料1は、クロム等の有
価金属の酸化が過大とならない温度(約700゜C)まで電
気炉3で二次予熱、すなわち仕上げ予熱される。このと
き電気炉5は、予熱された原料を溶解している状態にあ
る。この電気炉5による溶解が終了すると、電気炉3
は、加熱器4が取り外され、電極6が取り付けられる。
そして、電気炉3において、原料の溶解が開始される。
Stainless steel scrap or the like is first charged as a preheating raw material 1 into a bucket 2 and is primarily preheated to a temperature of 200 to 300 ° C. Next, the preheating raw material 1 is charged into the electric furnace 3. The electric furnace 3 includes a heater 4 that heats the preheating raw material 1 by burning fuel. The preheating raw material 1 is secondarily preheated, that is, finish preheated in the electric furnace 3 to a temperature (about 700 ° C.) at which oxidation of valuable metals such as chromium does not become excessive. At this time, the electric furnace 5 is in a state of melting the preheated raw material. When the melting in the electric furnace 5 is completed, the electric furnace 3
The heater 4 is removed and the electrode 6 is attached.
Then, the melting of the raw materials is started in the electric furnace 3.

電気炉3,5には、それぞれ炉内圧検出器7a,7bが設け
られており、電気炉3,5の炉内圧を検出する。この検
出値を設定値と比較し、該設定値となるように流量調整
弁8a,8bの開度を調整することにより、電気炉3,5の
炉内圧を設定値に維持することができる。
The electric furnaces 3 and 5 are provided with furnace pressure detectors 7a and 7b, respectively, and detect the furnace pressures of the electric furnaces 3 and 5. By comparing the detected value with a set value and adjusting the opening of the flow rate adjusting valves 8a, 8b so as to be the set value, the internal pressure of the electric furnaces 3, 5 can be maintained at the set value.

電気炉3及び電気炉5で発生した排ガスは、それぞれの
分岐ダクト9a,9bから集合ダクト10に集められ、バケッ
ト2に全量送り込まれる。集合ダクト10の途中には入側
弁11が設けられており、この入側弁11の前方の排ガスの
圧力を圧力検出器12で検出する。排ガスは、上方から下
方に向けてバケット2に送り込まれ、バケット2内の原
料を予熱した後、下部の排気ダクト13を経て排気ファン
14に送られる。なお、圧力検出器12は、入側弁11の後方
に設けても良い。
Exhaust gas generated in the electric furnace 3 and the electric furnace 5 is collected from the respective branch ducts 9a and 9b into the collecting duct 10 and sent to the bucket 2 in its entirety. An inlet valve 11 is provided in the middle of the collecting duct 10, and the pressure of the exhaust gas in front of the inlet valve 11 is detected by a pressure detector 12. The exhaust gas is sent from the upper side to the lower side into the bucket 2, preheats the raw material in the bucket 2, and then passes through the exhaust duct 13 in the lower portion to the exhaust fan.
Sent to 14. The pressure detector 12 may be provided behind the inlet valve 11.

また、電気炉の操業状態については、全ての炉が二次予
熱又は溶解状態にあるとは限らず、一部の炉は、原料装
入,加熱器4又は電極6の着脱,出鋼等の状態もある。
このようなとき、当該炉の流量調整弁8a又は8bを閉じ、
当該炉からは排ガスを吸引しない。また、何れの炉も二
次予熱又は溶解状態にない場合は、入側弁11及び出側弁
16を閉じ、バイパス弁18を開き、排気ファン14,20を低
速運転する。
Regarding the operating state of the electric furnace, not all of the furnaces are in the secondary preheating or melting state, and some of the furnaces include charging of raw materials, attachment / detachment of the heater 4 or the electrode 6, tapping, etc. There is also a state.
At such time, close the flow rate adjusting valve 8a or 8b of the furnace,
Exhaust gas is not drawn from the furnace. If neither furnace is in the secondary preheat or molten state, the inlet valve 11 and outlet valve
16 is closed, the bypass valve 18 is opened, and the exhaust fans 14 and 20 are operated at low speed.

排気ファン14は、回転数制御器15で回転数が制御され
る。この回転数制御器15は、前述の圧力検出器12で検出
されたバケット入側での排ガスの圧力が設定値となるよ
うに、排気ファン14の回転数を調節する。すなわち、多
量の排ガスがバケット2に送給され圧力が上昇するとき
には、排気ファン14の回転数を大きくして、多量の排ガ
スをバケット2から吸引して、バケット入側の圧力を一
定にする。他方、比較的少量の排ガスがバケット2に送
り込まれ圧力が低下するとき、排気ファン14の回転数を
下げ排ガスの吸引量を低減する。
The rotation speed of the exhaust fan 14 is controlled by the rotation speed controller 15. The rotation speed controller 15 adjusts the rotation speed of the exhaust fan 14 so that the exhaust gas pressure at the bucket entrance side detected by the pressure detector 12 described above becomes a set value. That is, when a large amount of exhaust gas is sent to the bucket 2 and the pressure rises, the rotation speed of the exhaust fan 14 is increased to suck a large amount of exhaust gas from the bucket 2 to make the pressure on the bucket inlet side constant. On the other hand, when a relatively small amount of exhaust gas is sent to the bucket 2 and the pressure drops, the rotation speed of the exhaust fan 14 is reduced to reduce the amount of exhaust gas suctioned.

したがって、電気炉3及び電気炉5で発生した排ガスの
全量がバケット2内における原料の予熱に利用され、排
熱が効率良く原料予熱に消費される。
Therefore, the entire amount of the exhaust gas generated in the electric furnace 3 and the electric furnace 5 is used for preheating the raw material in the bucket 2, and the exhaust heat is efficiently consumed for preheating the raw material.

また、集合ダクト10からバケット2を経由しないバイパ
ス管17が排気ダクト13に連絡され、このバイパス管17の
途中にバイパス弁18が設けられている。このバイパス管
17は、バケット2で予熱原料1を詰め替えるとき等の準
備期間中に使用される。すなわち、準備期間中において
は、入側弁11及び出側弁16を閉じ、バイパス弁18を開い
て、排ガスをバイパス管17に通し、バケット2をバイパ
スするように操作する。そして、排気ファン14を経た排
ガスは、集塵機19によって除塵された後、大気中に排出
される。
Further, a bypass pipe 17 that does not pass through the bucket 2 is connected to the exhaust duct 13 from the collecting duct 10, and a bypass valve 18 is provided in the middle of the bypass pipe 17. This bypass pipe
17 is used during a preparation period such as when the preheating raw material 1 is refilled in the bucket 2. That is, during the preparation period, the inlet valve 11 and the outlet valve 16 are closed, the bypass valve 18 is opened, the exhaust gas is passed through the bypass pipe 17, and the bucket 2 is bypassed. Then, the exhaust gas that has passed through the exhaust fan 14 is removed by the dust collector 19 and then discharged into the atmosphere.

なお、本例においては、排気ファン20を集塵機19の後方
にも設けて2基のファンとしている。しかし、排気ファ
ンは、集塵機19の前方又は後方に設けた1基だけでもよ
い。また、排気ファン14,20の回転数制御は、該排気フ
ァン14,20の双方又は一方のみについて行ってもよい。
In this example, the exhaust fan 20 is also provided behind the dust collector 19 to form two fans. However, only one exhaust fan may be provided in front of or behind the dust collector 19. The rotation speed control of the exhaust fans 14 and 20 may be performed on both or one of the exhaust fans 14 and 20.

このようにして、電気炉3及び電気炉5で発生した排ガ
スは、バケット2に全量送り込まれる。したがって、排
ガスの保有熱がバケット予熱に効率良く消費され、原料
の予熱を迅速に行うことができる。また、バケット入側
圧力が一定に維持され、電気炉の炉内圧変動が抑えられ
る結果、炉内圧上昇に伴う炉内からの発塵による建屋内
環境の悪化、又は炉内圧低下に伴う炉内への侵入空気に
よる熱効率の低下が抑制できる。
In this way, all the exhaust gas generated in the electric furnace 3 and the electric furnace 5 is sent to the bucket 2. Therefore, the retained heat of the exhaust gas is efficiently consumed for bucket preheating, and the raw material can be preheated quickly. In addition, the bucket inlet pressure is kept constant, and fluctuations in the furnace pressure of the electric furnace are suppressed.As a result, dust inside the furnace causes deterioration of the building environment due to the rise of the furnace pressure, or the inside pressure of the furnace decreases as the furnace pressure decreases. It is possible to suppress a decrease in thermal efficiency due to invading air.

〔実施例〕〔Example〕

第1図に示した装置を用いて、ステンレス鋼スクラップ
等をバケット2で一次予熱し、電気炉3で二次予熱し、
電気炉5では二次予熱されたスクラップを溶解している
とき、電気炉3及び電気炉5で発生した平均温度300゜C
の排ガスを、バケット入側圧力にして−200mm水柱に維
持してバケット2に送り込んだ。
Using the apparatus shown in FIG. 1, stainless steel scrap or the like is subjected to primary preheating in the bucket 2 and secondary preheating in the electric furnace 3,
In the electric furnace 5, when the secondary preheated scrap is melted, the average temperature generated in the electric furnace 3 and the electric furnace 5 is 300 ° C.
Of the exhaust gas was supplied to the bucket 2 while maintaining the pressure at the bucket inlet side to a water column of -200 mm.

この排ガスの流量は、最大時900Nm3/分、最小時300Nm3
/分であった。この排ガスの全量をバケット2に送り込
み予熱原料1の予熱を行ったところ、予熱時間60分で平
均温度270゜Cにスクラップを予熱することができた。こ
れに対し、比較例として、流量700Nm3/分を超える分の
排ガスについてはバケット2を迂回するバイパス管を経
由して集塵機19に流しながら、予熱原料1の予熱を行っ
たところ、予熱時間60分でスクラップの平均温度180゜C
であった。
The flow rate of this exhaust gas is 900 Nm 3 / min at maximum and 300 Nm 3 at minimum.
/ Min. When the entire amount of this exhaust gas was sent to the bucket 2 to preheat the preheating raw material 1, it was possible to preheat the scrap to an average temperature of 270 ° C in a preheating time of 60 minutes. On the other hand, as a comparative example, when the exhaust gas having a flow rate of 700 Nm 3 / min or more was flown to the dust collector 19 via the bypass pipe bypassing the bucket 2, the preheating raw material 1 was preheated, and the preheating time was 60 Average temperature of scrap 180 ° C in minutes
Met.

このように、本発明によれば、充分な熱量がバケット2
内の予熱原料1に供給されるため、廃熱を有効に利用し
て予熱原料1を高温まで予熱することができる結果、排
ガスの一部をバイパス管に逃がす方法と比べて排ガスの
保有熱の回収量が約50%向上した。また、電気炉の炉内
圧の変動も抑えられ、炉内からの発塵及び炉内への侵入
空気も抑制できた。更に、排ガスに浮遊しているダスト
の一部は、バケット2内の予熱原料1に捕捉された。し
たがって、排気ファン14から集塵機19に送られる排ガス
も、その分だけダスト含有率の少ないものとなり、集塵
機19の負荷が軽減した。
As described above, according to the present invention, a sufficient amount of heat is generated in the bucket 2.
Since it is supplied to the preheated raw material 1 inside, the preheated raw material 1 can be preheated to a high temperature by effectively utilizing the waste heat. As a result, compared with the method of releasing a part of the exhaust gas to the bypass pipe, Recovery amount improved by about 50%. In addition, fluctuations in the furnace pressure of the electric furnace were suppressed, and dust generation from the furnace and air entering the furnace could also be suppressed. Further, part of the dust floating in the exhaust gas was captured by the preheating raw material 1 in the bucket 2. Therefore, the exhaust gas sent from the exhaust fan 14 to the dust collector 19 also has a smaller dust content, and the load on the dust collector 19 is reduced.

〔発明の効果〕〔The invention's effect〕

以上に説明したように、本発明においては、電気炉で発
生した排ガスの全量をバケットに送り込み、原料の予熱
に使用している。そのため、排ガスの保有熱は、原料予
熱に有効に回収され、バケット予熱を迅速に行うこと及
びその予熱温度を高くすることが可能となる。また、排
ガスの流量及び温度の変動に対しては、バケットの出側
に設けられた排気ファンの回転数を調節することによっ
て吸収されるため、バケット入側圧力をほぼ一定に維持
して原料を予熱される。他方、電気炉では炉内圧の変動
が軽減され、操業条件を安定させることができる。そし
て、炉内圧を一定に維持するのに必要なだけの回転速度
で排気ファンを運転するため、消費電力も軽減できる。
更に、全量の排ガスがバケット内の原料層を通過するた
め、排ガスに浮遊しているダストがバケット内の原料に
捕捉され、集塵機に対する負荷も軽減される。このよう
にして、本発明によるとき、原料予熱時の排熱の回収効
率を高め、且つ電気炉の操業を安定させることができる
と共に、排ガスの処理が効果的に行われる。
As described above, in the present invention, the entire amount of exhaust gas generated in the electric furnace is sent to the bucket and used for preheating the raw material. Therefore, the retained heat of the exhaust gas is effectively recovered for the raw material preheating, and the bucket preheating can be quickly performed and the preheating temperature can be increased. Further, fluctuations in the flow rate and temperature of the exhaust gas are absorbed by adjusting the rotation speed of the exhaust fan provided on the outlet side of the bucket, so the bucket inlet pressure is maintained at a substantially constant level and the raw material is supplied. Preheated. On the other hand, in the electric furnace, fluctuations in the furnace pressure are reduced, and the operating conditions can be stabilized. Further, since the exhaust fan is operated at a rotation speed required to maintain the furnace pressure constant, power consumption can be reduced.
Furthermore, since the entire amount of exhaust gas passes through the raw material layer in the bucket, the dust floating in the exhaust gas is captured by the raw material in the bucket, and the load on the dust collector is also reduced. In this way, according to the present invention, the efficiency of recovering the exhaust heat at the time of preheating the raw material can be improved, the operation of the electric furnace can be stabilized, and the exhaust gas can be effectively treated.

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

第1図は、本発明に従った原料予熱を組み込んだ予熱か
ら溶解までの全体的なフローを示す図である。
FIG. 1 is a diagram showing an overall flow from preheating to melting in which raw material preheating according to the present invention is incorporated.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】バケット内で一次予熱した固形原料を電気
炉に投入して二次予熱し、次いで予熱された原料を前記
電気炉内で溶解又は精錬する際、前記電気炉を2基又は
それ以上配置し、その一部が二次予熱状態にあるとき残
りの電気炉を溶解又は精錬状態に置き、前記バケットに
至るダクトを経由して前記複数の電気炉で発生した排ガ
スを前記バケットに導き、前記ダクト内における排ガス
のバケット入側圧力に基づいて、前記バケットの出側に
接続された排気ダクトに設けられている排気ファンの回
転数を制御することを特徴とする排ガスを利用した原料
の予熱方法。
1. A solid raw material which is preheated in a bucket is charged into an electric furnace for secondary preheating, and when the preheated raw material is melted or refined in the electric furnace, two or more electric furnaces are used. Placed above, when a part of it is in the secondary preheating state, the rest of the electric furnace is placed in a melting or refining state, and the exhaust gas generated in the plurality of electric furnaces is guided to the bucket via a duct leading to the bucket. , Based on the bucket inlet side pressure of the exhaust gas in the duct, to control the rotation speed of the exhaust fan provided in the exhaust duct connected to the outlet side of the bucket of the raw material using the exhaust gas Preheating method.
JP5459088A 1988-03-07 1988-03-07 Preheating method for raw materials using exhaust gas Expired - Fee Related JPH0660794B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5459088A JPH0660794B2 (en) 1988-03-07 1988-03-07 Preheating method for raw materials using exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5459088A JPH0660794B2 (en) 1988-03-07 1988-03-07 Preheating method for raw materials using exhaust gas

Publications (2)

Publication Number Publication Date
JPH01230988A JPH01230988A (en) 1989-09-14
JPH0660794B2 true JPH0660794B2 (en) 1994-08-10

Family

ID=12974939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5459088A Expired - Fee Related JPH0660794B2 (en) 1988-03-07 1988-03-07 Preheating method for raw materials using exhaust gas

Country Status (1)

Country Link
JP (1) JPH0660794B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05322449A (en) * 1992-05-26 1993-12-07 Nippon Steel Corp Preheating control method in compound melting device
JP5130986B2 (en) * 2008-03-25 2013-01-30 横浜ゴム株式会社 Heat treatment furnace operation management system
JP6323286B2 (en) * 2014-09-30 2018-05-16 新日鐵住金株式会社 Exhaust heat recovery equipment for heating furnace and exhaust heat recovery method for heating furnace

Also Published As

Publication number Publication date
JPH01230988A (en) 1989-09-14

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