JPS5848834B2 - Arc furnace for melting reduced iron - Google Patents
Arc furnace for melting reduced ironInfo
- Publication number
- JPS5848834B2 JPS5848834B2 JP51073450A JP7345076A JPS5848834B2 JP S5848834 B2 JPS5848834 B2 JP S5848834B2 JP 51073450 A JP51073450 A JP 51073450A JP 7345076 A JP7345076 A JP 7345076A JP S5848834 B2 JPS5848834 B2 JP S5848834B2
- Authority
- JP
- Japan
- Prior art keywords
- carbon
- reduced iron
- molten steel
- basicity
- signal
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Discharge Heating (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
【発明の詳細な説明】
この発明は還元鉄を連続装入して溶解する還元鉄溶解用
アーク炉に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an arc furnace for melting reduced iron in which reduced iron is continuously charged and melted.
ア・−ク炉を用いる還元鉄製鋼法にネ・いては、最初に
全溶解量の10乃至30%のスクラップを炉に装入しこ
れをアークで溶解後、還元鉄を連続装入して溶解をおこ
なうので,還元鉄連続装入完了時点で所定の成分となる
よう操業するのが好筐しい。In the method of making reduced iron steel using an arc furnace, 10 to 30% of the total amount of scrap is first charged into the furnace, and after melting it in the arc, reduced iron is continuously charged. Since melting is carried out, it is best to operate the process so that the specified composition is achieved when the continuous charging of reduced iron is completed.
ところが還元鉄は酸化鉄として多量の酸素を含んでおり
、これが溶解の際溶鋼内の炭素分で還元されるので、ス
クラップ装入時に適量の炭素分を余分に入れる必要があ
り,この加炭量が適切でないと加炭や脱炭に要する時間
が長くなり1た過剰の加炭材から硫黄分が溶鋼に入り好
ましくない。However, reduced iron contains a large amount of oxygen as iron oxide, and this is reduced by the carbon in the molten steel during melting, so it is necessary to add an appropriate amount of extra carbon when charging the scrap, and the amount of carburization increases. If this is not appropriate, the time required for carburization and decarburization will be long, and sulfur content will enter the molten steel from the excess carburizer, which is undesirable.
普た還元鉄は酸性組戒の脈石を含んでいるため、酸性ス
ラグが生成され塩基比耐火物からなる炉壁の溶損が著し
いので、スラグの塩基度を適当範囲(通常1.25乃至
4)K維持する必要がある。Since reduced iron contains acidic gangue, acidic slag is produced and the furnace wall, which is made of basicity ratio refractories, is severely eroded. 4) It is necessary to maintain K.
さらに還元鉄の連続装入は電極通電状態の4%おこなう
が効率のよい溶解をおこなうには溶鋼混度が低下しない
よう一定範囲(通常1575℃〜1585℃)に維持す
る必要がある。Further, continuous charging of reduced iron is carried out at a rate of 4% when the electrode is energized, but in order to perform efficient melting, it is necessary to maintain the molten steel mixture within a certain range (usually 1575°C to 1585°C) so as not to decrease.
本発明は上記の点にかんがみてなされたもので、溶鋼中
の炭素量,スラグの塩基度、溶鋼湛度をすべて自動的に
制御し、最大溶解速度をもって効率的に所定成分の溶鋼
を得ることのできる還元鉄溶解用アーク炉を提供しよう
とするものである。The present invention has been made in view of the above points, and aims to automatically control all of the carbon content in molten steel, the basicity of slag, and the molten steel content to efficiently obtain molten steel with a predetermined composition at the maximum melting rate. The purpose of this invention is to provide an arc furnace for melting reduced iron that can be used to melt reduced iron.
以下、第1図によって本発明の一実施例を説明する。An embodiment of the present invention will be described below with reference to FIG.
図中,1はアーク炉の炉殼,2は炉蓋,3は電極、4は
溶鋼,5は溶融スラグ,11は先端を溶鋼に浸漬され所
定の短時間間隔をもって作動する試料採取器、12は試
料移送用のシュータ、13は分光分折などを応用した炭
素量測定器、14はオンオフ調節計で炭素量測定器の出
力信号を内部の炭素量上限設定値と比較してその偏差が
十のときオン信号を継続して発するもの、15はオンオ
フ調節計で炭素量測定器の出力信号を内部の炭素量下限
設定値と比較してその偏差が一のときオン信号を継続し
て発するもの、16.17は付勢されると開く電磁開閉
弁,18は炉内に連通する酸素吹込管、19は酸素供給
源に至る配管、20は炉内に連通する炭素粉吹込管,2
1は炭素粉供給源に至る配管である。In the figure, 1 is the furnace shell of the arc furnace, 2 is the furnace lid, 3 is the electrode, 4 is the molten steel, 5 is the molten slag, 11 is a sample collector whose tip is immersed in the molten steel and operates at predetermined short time intervals, 12 13 is a chute for transferring the sample, 13 is a carbon content measuring device that uses spectroscopic analysis, etc., and 14 is an on/off controller that compares the output signal of the carbon content measuring device with the internal carbon content upper limit setting value to ensure that the deviation is sufficient. 15 is an on-off controller that compares the output signal of the carbon content measuring device with the internal carbon content lower limit set value and continuously issues an on signal when the difference is one. , 16.17 is an electromagnetic on-off valve that opens when energized, 18 is an oxygen blowing pipe communicating with the inside of the furnace, 19 is a pipe leading to an oxygen supply source, 20 is a carbon powder blowing pipe communicating with the inside of the furnace, 2
1 is a pipe leading to a carbon powder supply source.
捷た31は先端を溶融スラグに浸漬され所定の短時間間
隔をもって作動する試料採取器、32は試料移送用シュ
ータ,33はスラグ塩基度測定器、34はオンオフ調節
計で塩基度測定器よりの出力信号を内部の塩基度設定値
と比較してその偏差が一のときオン信号を継続して発す
るもの、35は付勢されると開く電磁開閉弁,36は炉
内に連通ずる石灰装入用シュート,37は石灰用のホッ
パ,37aはその下端のノズル室、38は粉状の石灰、
39は先端にノズルを有する空気吹込管240は空気供
給源に至る配管である。31 is a sample collector whose tip is immersed in molten slag and operates at predetermined short time intervals, 32 is a chute for sample transfer, 33 is a slag basicity measuring device, and 34 is an on/off controller that operates from the basicity measuring device. A device that compares the output signal with the internal basicity setting value and continuously emits an on signal when the difference is 1, 35 is an electromagnetic on-off valve that opens when energized, and 36 is a lime charge that communicates with the inside of the furnace. 37 is a hopper for lime, 37a is a nozzle chamber at its lower end, 38 is a lime powder chute,
An air blowing pipe 240 having a nozzle at its tip is a pipe leading to an air supply source.
1た51は先端を溶鋼に浸漬され所定の短時間間隔で溶
鋼淵度を測定する熱電対形式の湿度検出器,52は温度
変換器、53は調節計で混度変換器の出力信号を内部の
漉度設定値と比較してその偏差が一のとき偏差量に比例
した数のパルスを発するもの、54は炉用変圧器,55
はこの変圧器に内蔵されたタップ切換器、56はタップ
切換器駆動用のパルスモータ,57はこのパルスモータ
に連結され最高電圧タップ切換時に信号を発するタップ
位置検出器,58はタップ位置検出器の出力信号により
閉路する切換スイッチ、59は調節計で温度変換器52
の出力信号を内部の混度設定値と比較しその偏差が一の
とき偏差量に比例した出力信号を継続して発するもの、
60は還元鉄装入最高速度に該当する信号を発する設定
器、61は演算器で設定器60の出力信号から調節計5
9の出力信号を減算するもの、62は直流増巾器,63
は還元鉄装入用ロータリーフイーダ64を駆動する直流
電動機,65は炉内に連通ずる還元鉄装入用シュート,
66は還元鉄用のホツパ67はペレット状の還元鉄であ
る。1, 51 is a thermocouple-type humidity detector whose tip is immersed in molten steel and measures the depth of molten steel at predetermined short intervals; 52 is a temperature converter; and 53 is a controller that internally receives the output signal of the mixture converter. 54 is a furnace transformer; 55 is a furnace transformer;
is a tap changer built into this transformer, 56 is a pulse motor for driving the tap changer, 57 is a tap position detector connected to this pulse motor and emits a signal when the highest voltage tap is changed, and 58 is a tap position detector. A selector switch 59 is a controller that closes the circuit according to the output signal of the temperature converter 52.
Compares the output signal with the internal mixture setting value, and when the deviation is one, continuously emits an output signal proportional to the amount of deviation,
60 is a setting device that emits a signal corresponding to the maximum reduced iron charging speed, and 61 is an arithmetic unit that uses the output signal of the setting device 60 to output a signal to the controller 5.
What subtracts the output signal of 9, 62 is a DC amplifier, 63
65 is a direct current motor that drives the rotary feeder 64 for charging reduced iron, and 65 is a chute for charging reduced iron that communicates with the inside of the furnace.
A hopper 66 for reduced iron 67 is a pellet-shaped reduced iron hopper.
すなわち、今スクラップの溶解が終了し、還元鉄の連続
装入が最高装入速度をもって開始されると,所定の短時
間間隔で試料採取器11が作動し,採取された試料はシ
ュータ12Vcより炭素量測定器13に移送され炭素量
の分析が自動的にむとなわれ炭素量に比例した信号がオ
ンオフ調節計1415に与えられる。That is, when the melting of the scrap is now completed and the continuous charging of reduced iron is started at the maximum charging speed, the sample collector 11 is operated at predetermined short intervals, and the collected sample is transferred to the carbon from the chute 12Vc. The carbon content is transferred to the quantity measuring device 13, where the carbon content is automatically analyzed and a signal proportional to the carbon content is given to the on/off controller 1415.
炭素量が所定の上限値を越えた場合はオンオフ調節計1
4よりオン信号が出され、電磁開閉弁16が開いて酸素
吹込管18よシ酸素が炉内に供給され、この供給は炭素
量が上限値以下になったことを検出する壕で続けられる
。If the carbon content exceeds the specified upper limit, turn on/off controller 1.
4, an on-signal is issued, the electromagnetic on-off valve 16 is opened, and oxygen is supplied into the furnace through the oxygen blowing pipe 18, and this supply is continued by a trench that detects that the amount of carbon has fallen below the upper limit.
1た炭素量が所定の下限値以下となった場合は上記と同
様にしてオンオフ調節計15よりオン信号が出され電磁
開閉弁11が開いて炭素粉吹込管20より炭素粉が炉内
に吹込1れる。When the amount of carbon is below the predetermined lower limit, an on-off signal is output from the on-off controller 15 in the same way as above, the electromagnetic on-off valve 11 is opened, and carbon powder is blown into the furnace from the carbon powder injection pipe 20. 1.
一方還元鉄連続装入開始により所定の短時間間隔で試料
採取器31が作動し採取されたスラグはシュータ32を
経て塩基度測定器33に移送され分析されてスラグ塩基
度に比例した信号がオンオフ調節計34K与えられ、塩
基度が所定値以下になるとオンオフ調節計34はオン信
号を発し,電磁開閉弁35が開いて空気吹込菅39よυ
の噴出空気によって石灰38がシュート36を経て炉内
に装入され,塩基度が所定値以上となったときのオンオ
フ調節計34よりのオフ信号により石灰装入は停止され
る。On the other hand, with the start of continuous charging of reduced iron, the sample collector 31 is activated at predetermined short intervals, and the sampled slag is transferred to the basicity measuring device 33 via the chute 32 and analyzed, and a signal proportional to the basicity of the slag is turned on and off. The controller 34K is applied, and when the basicity falls below a predetermined value, the on-off controller 34 issues an on signal, the electromagnetic shut-off valve 35 opens, and the air blowing tube 39 is opened.
Lime 38 is charged into the furnace through the chute 36 by the ejected air, and lime charging is stopped by an off signal from the on/off controller 34 when the basicity reaches a predetermined value or more.
筐た淵度検出器51およびこれに接続した温度変換器5
2Kよって検出された溶鋼湛度は所定の時間ごとに調節
計53の入力信号として与えられ,溶鋼温度が所定値よ
り低いとき調節計53はパルス信号を発し、パルスモー
タ56が作動してタップ切換器55が高電圧側に切換え
られる。Encased depth detector 51 and temperature converter 5 connected to it
The molten steel content detected by the 2K is given as an input signal to the controller 53 at predetermined intervals, and when the molten steel temperature is lower than the predetermined value, the controller 53 emits a pulse signal, and the pulse motor 56 operates to change the tap. 55 is switched to the high voltage side.
タップ切換器55が最高電圧位置に切換えられるとタッ
プ切換器は機械的,電気的にロックされ、一方タップ位
置検出器57が出力を発して切換スイッチ58を導通状
態に切換える。When the tap changer 55 is switched to the highest voltage position, the tap changer is mechanically and electrically locked, while the tap position detector 57 provides an output to switch the transfer switch 58 into a conductive state.
溶鋼淵度が依然として設定値以下のときは調節計59は
温度変換器52よりの信号と設定値との偏差量に比例し
た出力信号を発し、この信号は演算器61において設定
器60の出力信号から減算されるので直流増巾器62の
入力信号が減少し、直流電動機63の電機子電圧が低下
してロータリーフイーダ64の回転数が低下し還元鉄の
装入量減少により溶鋼淵度は上昇方向に制御される。When the depth of molten steel is still below the set value, the controller 59 emits an output signal proportional to the deviation between the signal from the temperature converter 52 and the set value, and this signal is converted to the output signal of the setting device 60 in the calculator 61. Since the input signal to the DC amplifier 62 decreases, the armature voltage of the DC motor 63 decreases, the rotation speed of the rotary leaf feeder 64 decreases, and the amount of charged reduced iron decreases, so the molten steel depth decreases. Controlled in the upward direction.
溶鋼温度が上昇すれば設定値との偏差が減少し,調節計
59よシの減算信号が減少し直流電動機の回転数は増加
し、溶鋼湛度が設定値以上となれば減算信号はOとなり
、還元鉄は設定器60の設定値により所定の最高速度で
連続装入される。As the molten steel temperature rises, the deviation from the set value decreases, the subtraction signal from the controller 59 decreases, and the rotational speed of the DC motor increases, and when the molten steel content exceeds the set value, the subtraction signal becomes O. The reduced iron is continuously charged at a predetermined maximum speed according to the setting value of the setting device 60.
次に第2図はこの発明の他の実施例を示し,溶鋼淵度制
御関係部分のみを示し他の部分は図示を省略したが第1
図と同様とする。Next, FIG. 2 shows another embodiment of the present invention, showing only the parts related to molten steel depth control and omitting the illustration of other parts.
Same as the figure.
この実施例は第1図に示す実施例における調節計53,
タップ位置検出器5γ,切換スイッチ58とこれらの間
の結線を省略して混度変換器52の出力信号が直接調節
計59のみに与えられるようにしたもので,タップ切換
器55は他の操作によりたとえば最高電圧位置に維持し
た捷Σで溶解をおこなう。This embodiment differs from the controller 53 in the embodiment shown in FIG.
The tap position detector 5γ, the changeover switch 58, and the connection between them are omitted so that the output signal of the mixture converter 52 is directly given only to the controller 59, and the tap changer 55 is used for other operations. For example, melting is performed with the switch Σ maintained at the highest voltage position.
この場合は溶鋼湿度調節はロータリーフイーダ64の回
転数制御のみにておこなうもので、装置が簡略化される
。In this case, the molten steel humidity is controlled only by controlling the rotation speed of the rotary feeder 64, which simplifies the apparatus.
なお上記各実施例は溶鋼中の炭素量、スラグの塩基度お
よび溶鋼温度の検出を所定の短時間間隔でおこなうもの
であるが、混度釦よび成分の連続検出器を用いて,各検
出器からの連続信号により各操作部を連続的に制御する
ようにしてもよい。In each of the above embodiments, the amount of carbon in molten steel, the basicity of slag, and the temperature of molten steel are detected at predetermined short intervals. Each operating section may be continuously controlled by continuous signals from the controller.
壕た電磁開閉弁16.17.35はオンオフ制御以外に
偏差に応じて開度を調整するようにしてもよい。The recessed electromagnetic on-off valves 16, 17, and 35 may be configured to have their opening degrees adjusted in accordance with deviations in addition to on/off control.
さらに炭素供給源としては炭素粉を用いるほか,炭素戒
分を多く含んだ溶鋼を炉内に注入して用いてもよい。Furthermore, in addition to using carbon powder as a carbon supply source, molten steel containing a large amount of carbon may be injected into the furnace.
以上説明したとおり、この発明は還元鉄連続装入中にお
いて溶鋼中の炭素量、スラグの塩基度、溶鋼湿度をそれ
ぞれ所定時間間隔をおいてあるいは連続的に検出し、所
定の各設定値と比較しその偏差に応じて酸素供給装置、
炭素供給装置および石灰装入装置の作動、還元鉄装入速
度の加減1たは変圧器のタップ切換と還元鉄装入速度の
加減を、いずれも自動的K釦こなうようにしたので、還
元鉄連続装入中における溶鋼中の炭素量、スラグの塩基
度、溶鋼温度がそれぞれ所定の範囲に正確かつ容易に維
持され、溶解中あるいは溶解後の大規模な加炭や脱炭が
不要となり,塩基比スラグによる炉壁損耗がなくなり炉
壁補修時間が減るとともに,設備の有する最高溶解速度
による高能率の溶解作業をむこなうことができ、もって
生産能率向上および省力化の効果が得られる。As explained above, the present invention detects the amount of carbon in molten steel, the basicity of slag, and the humidity of molten steel at predetermined time intervals or continuously during continuous charging of reduced iron, and compares them with each predetermined set value. Oxygen supply device according to the deviation,
The operation of the carbon supply device and lime charging device, the adjustment of the reduced iron charging speed, the tap switching of the transformer, and the adjustment of the reduced iron charging speed are all automatically controlled by the K button. During continuous charging of reduced iron, the amount of carbon in the molten steel, the basicity of the slag, and the molten steel temperature are accurately and easily maintained within specified ranges, eliminating the need for large-scale carburization or decarburization during or after melting. , Furnace wall damage due to base ratio slag is eliminated, furnace wall repair time is reduced, and high-efficiency melting work can be performed with the highest melting speed of the equipment, resulting in improved production efficiency and labor savings. .
第1図はこの発明の一実施例を示す系統図、第2図はこ
の発明の他の実施例を示す要部系統図である。
1・・・炉殼、11・・・試料採取器、12・・・シュ
ータ,13・・・炭素量測定器、14.15・・・オン
オフ調節計,16.17・・・電磁開閉弁,18・・・
酸素吹込管、20・・・炭素粉吹込管,31・・・試料
採取器,32・・・シュータ,33・・・スラグ塩基度
測定器,34・・・オンオフ調節計,35・・・電磁開
閉弁,36・・・石灰装入用シュート,39・・・空気
吹込管,51・・・温度検出器、52・・・温度変換器
、53・・・調節計,54・・・炉用変圧器,55・・
・タップ切換器,56・・・パルスモータ、57・・・
タップ位置検出器,58・・・切換スイッチ,59・・
・調節計、60・・・設定器,61・・・演算器,62
・・・直流増巾器,63・・・直流電動機、64・・・
ロータリーフイーダ,65・・・還元鉄装入用シュート
。FIG. 1 is a system diagram showing one embodiment of this invention, and FIG. 2 is a system diagram of main parts showing another embodiment of this invention. DESCRIPTION OF SYMBOLS 1... Furnace shell, 11... Sample collector, 12... Shooter, 13... Carbon content measuring device, 14.15... On/off controller, 16.17... Solenoid shut-off valve, 18...
Oxygen blowing pipe, 20... Carbon powder blowing pipe, 31... Sample collector, 32... Shooter, 33... Slag basicity measuring device, 34... On/off controller, 35... Electromagnetic Opening/closing valve, 36... Chute for lime charging, 39... Air blowing pipe, 51... Temperature detector, 52... Temperature converter, 53... Controller, 54... For furnace Transformer, 55...
・Tap changer, 56...Pulse motor, 57...
Tap position detector, 58... changeover switch, 59...
・Controller, 60... Setting device, 61... Arithmetic unit, 62
...DC amplifier, 63...DC motor, 64...
Rotary feeder, 65...Chute for charging reduced iron.
Claims (1)
よび炭素供給装置と,炉内に石灰および還元鉄を装入す
る石灰装入装置および還元鉄連続装入装置とをそなえた
還元鉄溶解用アーク炉に釦いて、還元鉄連続装入中に連
続的筐たは所定時間間隔をおいて溶鋼中の炭素量,スラ
グの塩基度および溶鋼の混度をそれぞれ検出する炭素量
検出器、塩基度検出器および溶鋼温度検出器と,上記炭
素量検出器の検出信号と設定値とを比較し炭素量が所定
の上限値以上のとき上記酸素供給装置を作動させる信号
を発し,炭素量が所定の下限値以下のとき上記炭素供給
装置を作動させる信号を発する炭素量制御装置と、上記
塩基度検出器の検出信号と設定値とを比較し塩基度が所
定値以下のとき上記石灰装入装置を作動させる信号を発
する塩基度制御装置と,上記溶鋼温度検出器の検出信号
と設定値とを比較し溶鋼湛度が所定値以下のとき上記還
元鉄連続装入装置の単位時間当りの装入量を減少させる
信号を発する溶鋼湛度制御装置とをそなえたことを特徴
とする還元鉄溶解用アーク炉。 2 炉内に酸素および炭素分を供給する酸素供給装置お
よび炭素供給装置と,炉内に石灰および還元鉄を装入す
る石灰装入装置および還元鉄連続装入装置とをそなえ、
タップ切換器付炉用変圧器に接続された還元鉄溶解用ア
ーク炉において,還元鉄連続装入中に連続的筐たは所定
時間間隔をおいて溶鋼中の炭素量,スラグの塩基度およ
び溶鋼の混度なそれぞれ検出する炭素量検出器,塩基度
検出器および溶鋼湿度検出器と、上記炭素量検出器の検
出信号と設定値とを比較し炭素量が所定の上限値以上の
とき上記酸素供給装置を作動させる信号を発し、炭素量
が所定の下限値以下のとき上記炭素供給装置を作動させ
る信号を発する炭素量制御装置と、上記塩基度検出器の
検出信号と設定値とを比較し塩基度が所定値以下のとき
上記石灰装入装置を作動させる信号を発する塩基度制御
装置と、上記溶鋼温度検出器の検出信号と設定値とを比
較し溶鋼温度が所定値以下のとき上記タップ切換器を高
電圧側に切換える信号を発し、最高電圧に切換後は上記
還元鉄連続装入装置の単位時間当りの装入量を減少させ
る信号を発する溶鋼温度制御装置とをそなえたことを特
徴とする還元鉄溶解用アーク炉。[Scope of Claims] 1. An oxygen supply device and a carbon supply device that supply oxygen and carbon into the furnace, and a lime charging device and a continuous reduced iron charging device that charge lime and reduced iron into the furnace. A carbon detector is used to detect the amount of carbon in molten steel, the basicity of slag, and the mixture of molten steel continuously or at predetermined time intervals during continuous charging of reduced iron by pressing a button on the arc furnace equipped for melting reduced iron. A quantity detector, a basicity detector, a molten steel temperature detector, and a detection signal of the carbon quantity detector are compared with a set value, and when the carbon quantity is above a predetermined upper limit value, a signal is issued to operate the oxygen supply device. , a carbon amount control device that emits a signal to operate the carbon supply device when the carbon amount is below a predetermined lower limit value, and a detection signal of the basicity detector and a set value are compared, and when the basicity is below a predetermined value; A basicity control device that issues a signal to operate the lime charging device and a detection signal of the molten steel temperature detector are compared with a set value, and when the molten steel content is below a predetermined value, the unit of the continuous reduced iron charging device is An arc furnace for melting reduced iron, characterized in that it is equipped with a molten steel saturation control device that issues a signal to reduce the charging amount per hour. 2. Equipped with an oxygen supply device and a carbon supply device that supply oxygen and carbon into the furnace, and a lime charging device and a continuous reduced iron charging device that charge lime and reduced iron into the furnace,
In an arc furnace for melting reduced iron connected to a furnace transformer with a tap changer, carbon content in molten steel, basicity of slag, and molten steel are measured continuously or at predetermined time intervals during continuous charging of reduced iron. The carbon content detector, basicity detector, and molten steel humidity detector each detect a mixture of Compare the detection signal of the basicity detector and the set value with a carbon amount control device that emits a signal to activate the feeding device and when the carbon amount is below a predetermined lower limit value, a signal to activate the carbon feeding device. A basicity control device that issues a signal to operate the lime charging device when the basicity is below a predetermined value, and a basicity control device that compares the detection signal of the molten steel temperature detector with a set value and operates the tap when the molten steel temperature is below a predetermined value. It is characterized by being equipped with a molten steel temperature control device that issues a signal to switch the switching device to the high voltage side, and after switching to the highest voltage, issues a signal to reduce the charging amount per unit time of the continuous reduced iron charging device. Arc furnace for melting reduced iron.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51073450A JPS5848834B2 (en) | 1976-06-21 | 1976-06-21 | Arc furnace for melting reduced iron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51073450A JPS5848834B2 (en) | 1976-06-21 | 1976-06-21 | Arc furnace for melting reduced iron |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52156110A JPS52156110A (en) | 1977-12-26 |
| JPS5848834B2 true JPS5848834B2 (en) | 1983-10-31 |
Family
ID=13518566
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51073450A Expired JPS5848834B2 (en) | 1976-06-21 | 1976-06-21 | Arc furnace for melting reduced iron |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5848834B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995009336A1 (en) * | 1993-09-30 | 1995-04-06 | Ishikawajima-Harima Jukogyo Kabushiki Kaisha | Electric arc fusion furnace |
-
1976
- 1976-06-21 JP JP51073450A patent/JPS5848834B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995009336A1 (en) * | 1993-09-30 | 1995-04-06 | Ishikawajima-Harima Jukogyo Kabushiki Kaisha | Electric arc fusion furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52156110A (en) | 1977-12-26 |
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