JP2526554B2 - Dissolution control method for AC arc furnace - Google Patents
Dissolution control method for AC arc furnaceInfo
- Publication number
- JP2526554B2 JP2526554B2 JP61195632A JP19563286A JP2526554B2 JP 2526554 B2 JP2526554 B2 JP 2526554B2 JP 61195632 A JP61195632 A JP 61195632A JP 19563286 A JP19563286 A JP 19563286A JP 2526554 B2 JP2526554 B2 JP 2526554B2
- Authority
- JP
- Japan
- Prior art keywords
- phase
- melting
- electrode
- arc furnace
- arc
- 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
Links
- 238000000034 method Methods 0.000 title claims description 12
- 238000004090 dissolution Methods 0.000 title description 5
- 238000002844 melting Methods 0.000 claims description 41
- 230000008018 melting Effects 0.000 claims description 41
- 238000001514 detection method Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000005526 G1 to G0 transition Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
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
- Y02P10/25—Process efficiency
Landscapes
- Discharge Heating (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は交流アーク炉の溶解制御法、特に不均等溶
解の防止化に関する。TECHNICAL FIELD The present invention relates to a melting control method for an AC arc furnace, and more particularly to prevention of uneven melting.
〔従来の技術〕 三相交流アーク炉では炉に給電する銅管、可とうケー
ブル、電極等変圧器の二次側導体の持つインピーダンス
によつて炉の電気特性が決定される。この二次側導体は
配置上不平衡が避けられず、各相のインピーダンスを全
く同じにすることは非常に困難であり、ほとんど不可能
である。このため各相の電極で発生するアークは同一と
ならず、電力が多く入る相(以下、激動相という。)と
電力が少く入る相(以下、静止相という。)を生じ溶解
が不均等になつている。[Prior Art] In a three-phase AC arc furnace, the electrical characteristics of the furnace are determined by the impedance of the copper tube feeding the furnace, the flexible cable, the secondary conductor of the transformer such as the electrode. An imbalance is unavoidable in the arrangement of the secondary side conductor, and it is very difficult to make the impedances of the respective phases exactly the same, and it is almost impossible. Therefore, the arcs generated at the electrodes of each phase are not the same, and a phase in which a large amount of power is input (hereinafter referred to as a turbulent phase) and a phase in which a small amount of power is input (hereinafter referred to as a stationary phase) are generated, resulting in uneven melting. I'm running.
激動相では早くスクラツプが溶け、炉壁への熱損失あ
るいは炉壁の損傷など不利になる一方静止相では溶解が
遅れるため生産性低下の原因となつている。In the turbulent phase, the scrap quickly melts, which is disadvantageous such as heat loss to the furnace wall or damage to the furnace wall, but in the stationary phase, melting is delayed, which causes a decrease in productivity.
炉内の溶解の不均等は上記供給電力の不均等以外にも
炉内の酸素濃度の不均等、スクラツプの入り具合、集塵
口の位置等などによつても引きおこされ、原単位及び生
産性の面でも問題となつている。The uneven melting in the furnace is caused not only by the uneven power supply but also by the uneven oxygen concentration in the furnace, the condition of the scrap, the position of the dust collection port, etc. It is also a problem in terms of sex.
この溶解の不均等を解決するために、従来は三相の各
相に流す電流を個別に変えて各相の電力の均等化を図る
方法や、各相毎に変圧器のタツプ電圧を個別に変えて調
整する方法が用いられている。In order to solve this inequality of melting, conventionally, the current flowing through each of the three phases is individually changed to equalize the power of each phase, or the tap voltage of the transformer is individually adjusted for each phase. A method of changing and adjusting is used.
上記従来の各線電流を変えて溶解の不均衡を調整する
方法においては、線電流を可変する範囲が炉用変圧器の
最大電流を超えることができないため、各相の電流を変
えようとすると電流を低減させて選ばざるを得なく、こ
のため全体の投入電力が減少し生産性の低下をきたし、
かつ電流を減らした電極のアークが不安定となつてしま
う。また炉用変圧器の利用率が悪く、調整巾も狭くなる
という問題点があつた。さらに各相に不平衡電流が流れ
るという問題点もある。In the conventional method of adjusting the imbalance of melting by changing each line current, the range in which the line current can be varied cannot exceed the maximum current of the furnace transformer. To reduce the total input power, resulting in lower productivity.
In addition, the arc of the electrode with reduced current becomes unstable. Moreover, the utilization rate of the transformer for the furnace is poor, and the adjustment range is narrowed. Further, there is a problem that an unbalanced current flows in each phase.
また、電圧を各相毎に変える方法においても、電圧の
可変範囲は炉用変圧器の最高電圧を超えることができな
いので、電圧を低減させて選ぶため投入電力が減少し、
炉用変圧器の利用率が悪く調整巾も狭くなるという問題
点があつた。また炉用変圧器のタツプ切換機構が複雑と
なり信頼性の低下を招き保守でも不利であつた。さらに
この場合も電源からみて不平衡電流を供給するという問
題点もある。Further, even in the method of changing the voltage for each phase, the variable range of the voltage cannot exceed the maximum voltage of the furnace transformer, so the input power is reduced because the voltage is selected to be reduced,
There was a problem that the utilization rate of the transformer for the furnace was poor and the adjustment range was narrow. In addition, the tap switching mechanism of the transformer for the furnace becomes complicated, resulting in a decrease in reliability, which is disadvantageous for maintenance. Also in this case, there is also a problem that an unbalanced current is supplied from the viewpoint of the power supply.
この発明はかかる問題点を解決するためになされたも
のであり、各相に流れる電流を均一にしながら不均等溶
解を補正することができる交流アーク炉の溶解制御法を
提案することを目的とするものである。The present invention has been made to solve the above problems, and an object of the present invention is to propose a melting control method for an AC arc furnace that can correct uneven melting while making the current flowing through each phase uniform. It is a thing.
この発明に係る交流アーク炉の溶解制御法は、三相交
流アーク炉の溶解速度の変化に対応して電極のアーク長
を変化させて溶解を促進するとき、特定の自己インダク
タンス及び相互インダクタンスを有する給電回路の各相
に個別に設けた調整可能な可変リアクトルによって、給
電回路の各相から各電極に流れる電流を一定にしながら
各相の電極に必要とする投入電力量に応じて上記可変リ
アクトルを調整する。The melting control method for an AC arc furnace according to the present invention has a specific self-inductance and mutual inductance when the arc length of an electrode is changed in response to a change in the melting rate of a three-phase AC arc furnace to promote melting. Adjustable variable reactors provided individually for each phase of the power supply circuit keep the current flowing from each phase of the power supply circuit to each electrode constant while adjusting the variable reactor according to the amount of input power required for the electrodes of each phase. adjust.
また、給電回路各相の1相以上に固定リアクトルを設
けて溶解の遅いまたは早い特性を有する相をなくするよ
うに溶解速度を平均化した三相交流アーク炉の溶解速度
の変化に対応して電極のアーク長を変化させて溶解を促
進するとき、特定の自己インダクタンス及び相互インダ
クタンスを有する給電回路の各相から各電極に流れる電
流を一定にするように給電回路各相に個別に設けた調整
可能な可変リアクトルによって、各相の電極に必要とす
る投入電力量に応じて上記可変リアクトルを調整する。
さらに、前記給電回路の力率cosθを0.9以下に設定する
ものである。In addition, in order to eliminate the phase having slow or fast melting characteristics by providing a fixed reactor on one or more of each phase of the power supply circuit, the melting rate is averaged to cope with changes in the melting rate of the three-phase AC arc furnace. When the arc length of the electrodes is changed to promote melting, adjustment is provided individually for each phase of the power supply circuit so that the current flowing from each phase of the power supply circuit having a specific self-inductance and mutual inductance is constant. With the possible variable reactor, the variable reactor is adjusted according to the amount of input electric power required for the electrodes of each phase.
Further, the power factor cos θ of the power supply circuit is set to 0.9 or less.
この発明においては三相交流アーク炉の溶解速度の変
化に対応して電極のアーク長を変化させてアーク抵抗を
変化させて溶解を促進するとき、各相に設けた可変リア
クトルを調整することにより各相に流れる電流の平衡を
保ちながら各相の投入電力を調整する。すなわち、溶解
の不均一性に従って各相に必要な投入比率と電力量に対
応した各相のアーク長に変化させる。前記各相のアーク
長を変化させたとき、各相の可変リアクトルのインダク
タンスを変化させて各相の投入電力量を調整するので、
インピーダンスバランスをとることが可能で、溶解が均
一になるように制御できる。また、三相交流各相に設け
た固定リアクトルにより常に溶解の速い相や遅い相があ
る場合、平均的な均等溶解ができるように調整する。さ
らに、給電回路はその力率cosθを0.9以下に設定するこ
とにより、アークが安定した状態で操業できる。In the present invention, when the arc length of the electrode is changed in response to the change in the melting rate of the three-phase AC arc furnace to change the arc resistance and promote the melting, by adjusting the variable reactor provided in each phase, The input power of each phase is adjusted while maintaining the balance of the current flowing in each phase. That is, the arc length of each phase is changed according to the charging ratio and the amount of electric power required for each phase according to the nonuniformity of melting. When the arc length of each phase is changed, the input electric energy of each phase is adjusted by changing the inductance of the variable reactor of each phase.
Impedance can be balanced and the dissolution can be controlled to be uniform. In addition, when there is a fast-dissolving phase or a slow-dissolving phase by the fixed reactors provided in each of the three-phase alternating current phases, adjustment is performed so that an average uniform dissolution can be performed. Furthermore, the power supply circuit can be operated in a stable arc state by setting the power factor cos θ to 0.9 or less.
第1図はこの発明の一実施例を示す回路図であり、図
においてEi(但しi=1,2,3)はY接続の三相交流電源
における各相の電源電圧、Liは炉回路各相の自己インダ
クタンス、Mijは炉回路各相間の相互インダクタンス、R
iは各相の全抵抗であり、各相の全抵抗Riは炉回路各相
の抵抗Rfiとアーク抵抗Raiとからなる。FIG. 1 is a circuit diagram showing an embodiment of the present invention, in which Ei (where i = 1, 2, 3) is a power supply voltage of each phase in a Y-connected three-phase AC power supply, and Li is a furnace circuit. Phase self-inductance, Mij is mutual inductance between furnace circuit phases, R
i is the total resistance of each phase, and the total resistance Ri of each phase consists of the resistance Rfi of each phase of the furnace circuit and the arc resistance Rai.
Lviは各相に各々付加された可変リアクトルであり、
可変リアクトルLviを個別に変えることにより各相のリ
アクタンス値を個別に変えることができる。またEbは炉
内溶融金属の対地電位である。Lvi is a variable reactor added to each phase,
The reactance value of each phase can be changed individually by changing the variable reactor Lvi individually. Eb is the ground potential of the molten metal in the furnace.
まず、上記のように構成した交流アーク炉の炉回路に
おいて各相に入れる可変リアクトルLviの値を決定する
原理を説明する。First, the principle of determining the value of the variable reactor Lvi put in each phase in the furnace circuit of the AC arc furnace configured as described above will be described.
第1図に示す回路においては各相に流れる電流をIi
(i=1〜3)とすると次の連立方程式が成立する。In the circuit shown in FIG. 1, the current flowing in each phase is Ii
(I = 1 to 3), the following simultaneous equations hold.
但し、ω=2πf,fは電源周波数である。ここで相順
位を正とし、I1とE1を基準とすると と表わせる。 However, ω = 2πf, f is the power supply frequency. Here, if the phase order is positive and I 1 and E 1 are the criteria, Can be expressed as
上記(1),(2)式より次の式が得られる。 From the above equations (1) and (2), the following equation is obtained.
(3)式より −b=R1+jω(Lv1+L1)+jωM12a2+jωM31a
…(4) a2−b=jωM12+R2a2+jω(Lv2+L2)a2+jωM
23a …(5) a−b=jωM31+jωM23a2+R3a+jω(Lv3+L3)
a …(6) (4),(5)式より (1−a2)=R1+jω(Lv1+L1−M12)+{−R2+j
ω(M12−Lv2−L2)}a2+jω(M31+M23)a …(7) インピーダンスには抵抗R分とインダクタンスL分が
含まれており、抵抗R分として各相の平均抵抗をとりイ
ンダクタンスL分として各相の平均インダクタンスをと
ると、 と表はせる。 From equation (3), −b = R 1 + jω (Lv 1 + L 1 ) + jωM 12 a 2 + jωM 31 a
(4) a 2 −b = jωM 12 + R 2 a 2 + jω (Lv 2 + L 2 ) a 2 + jωM
23 a (5) a−b = jωM 31 + jωM 23 a 2 + R 3 a + jω (Lv 3 + L 3 )
a (6) From equations (4) and (5), (1-a 2 ) = R 1 + jω (Lv 1 + L 1 −M 12 ) + {− R 2 + j
ω (M 12 −Lv 2 −L 2 )} a 2 + jω (M 31 + M 23 ) a (7) The impedance includes the resistance R and the inductance L, and the average of each phase is the resistance R. Taking the resistance and the inductance L, and taking the average inductance of each phase, Can be expressed as
上記(7)式に(8)式を代入し展開することにより
可変リアクトルLv2が次式で得られる。By substituting the equation (8) into the equation (7) and expanding it, the variable reactor Lv 2 is obtained by the following equation.
一方、第1図に示した炉回路に投入される全投入電力
Pは P=(R1+R2+R3)I2 …(10) となり、各電極への電力の配分はR1:R2:R3の比とな
る。そして各電極電流は等しいので、アーク電圧は各相
でRa1・I,Ra2・I,Ra3・Iとなり、溶解の遅い電極はア
ーク抵抗を大きくし、すなわちアーク長を長くして溶解
を促進する。 On the other hand, the total input power P input to the furnace circuit shown in FIG. 1 is P = (R 1 + R 2 + R 3 ) I 2 (10), and the power distribution to each electrode is R 1 : R 2 : It becomes the ratio of R 3 . And since the electrode currents are the same, the arc voltage becomes Ra 1 · I, Ra 2 · I, Ra 3 · I in each phase, and the electrode with slow melting increases the arc resistance, that is, lengthens the arc length to melt. Facilitate.
また、回路力率cosθは各相の負荷に加えられる電圧
をEとすると で表わされ、この回路力率cosθはアークが不安定にな
らないようcosθ<0.9に設定する。In addition, the circuit power factor cos θ is E when the voltage applied to the load of each phase is E This circuit power factor cosθ is set to cosθ <0.9 so that the arc does not become unstable.
いま、変圧器のタツプ電圧をE′とし必要な投入電力
量Pとアークの安定性を考慮した力率cosθが決められ
ると、各相電流I,各相の平均インダクタンスL及び全抵
抗R1+R2+R3は次式で決めることができる。Now, assuming that the tap voltage of the transformer is E ′ and the power factor cos θ that takes into account the required input power P and arc stability is determined, the current I of each phase, the average inductance L of each phase and the total resistance R 1 + R 2 + R 3 can be determined by the following formula.
また、各相への投入電力はR1I2:R2I2:R3I2の比とな
るので溶解に応じた各相への必要な投入比率を設定する
ことによつてR1,R2,R3の値が定まる。これらの値を用
いることにより(9)式により各相に付加した可変リア
クトルLv1,Lv2,Lv3の値を決めることができる。すな
わち溶解の進捗不均一性を炉内観察や炉壁の熱負荷レベ
ルなどによつて検出し、各相への必要な投入比率を設定
し各相の可変リアクトルを調整して溶解が均一になるよ
うに制御する。 Also, the power input to each phase is the ratio of R 1 I 2 : R 2 I 2 : R 3 I 2 , so by setting the necessary input ratio to each phase according to melting, R 1 , The values of R 2 and R 3 are determined. By using these values, the values of the variable reactors Lv 1 , Lv 2 , and Lv 3 added to each phase can be determined by the equation (9). In other words, the unevenness of melting progress is detected by observing the inside of the furnace and the heat load level of the furnace wall, setting the required input ratio to each phase, and adjusting the variable reactor of each phase to make the melting uniform. To control.
なお、可変リアクトルLv1,Lv2,Lv3を演算する
(9)式におけるインダクタンス分 の各値は次の方法により実測算出することができる。In addition, the inductance component in the equation (9) for calculating the variable reactors Lv 1 , Lv 2 , and Lv 3 Each value of can be measured and calculated by the following method.
アークが安定している溶解末期あるいは精錬期に可変
リアクトルLv1,Lv2,Lv3を切りはなして各相の電流が
同じになるように電極位置を調整し、各相への投入電力
Piを計測する。この計測した投入電力Piにより Pi=Ri・I2(i=1〜3) …(13) に基づき各相の抵抗Riを求め、この抵抗Riにより例えば
第1相の場合を例にとると によつて実測算出することができる。At the end of melting or refining when the arc is stable, the variable reactors Lv 1 , Lv 2 and Lv 3 are cut off and the electrode position is adjusted so that the current in each phase is the same, and the power input to each phase is adjusted.
Measure Pi. Based on this measured input power Pi, the resistance Ri of each phase is obtained based on Pi = Ri · I 2 (i = 1 to 3) (13), and for example the case of the first phase is taken from this resistance Ri. It is possible to actually measure and calculate.
第2図は上記原理により溶解制御を行なう交流アーク
炉の構成を示し、図において1は電源、2は電源1に接
続された炉用開閉器、3は炉用変圧器、4は炉用変圧器
3の二次側の各相に個別に接続した可変リアクトルであ
り、可変リアクトル4にはインダクレンスを可変するた
めのタツプが設けられている。5は二次側各相の電圧を
個別に検出する電圧検出回路、6は各相の電流を個別に
検出する電流検出回路、7は電極、8は炉本体である。
9は各相の電極7にそれぞれ取付けられた電極昇降装
置、10は炉本体8に取付けられた炉況センサ、11は電圧
検出回路5、電流検出回路6及び炉況センサ10からの情
報により電極昇降装置9、可変リアクタンス4及び炉用
変圧器3を調整する制御装置であり、制御装置11には第
3図に示すように電力量演算回路12、投入比率設定回路
13、アーク長演算回路14及びインダクタンス演算回路15
を備えている。FIG. 2 shows the configuration of an AC arc furnace that controls melting according to the above principle. In the figure, 1 is a power source, 2 is a switch for a furnace connected to the power source 1, 3 is a transformer for a furnace, and 4 is a transformer for a furnace. It is a variable reactor that is individually connected to each phase on the secondary side of the container 3, and the variable reactor 4 is provided with a tap for varying the induction. Reference numeral 5 is a voltage detection circuit that individually detects the voltage of each secondary side phase, 6 is a current detection circuit that individually detects the current of each phase, 7 is an electrode, and 8 is a furnace body.
Reference numeral 9 is an electrode lifting device attached to each phase electrode 7, 10 is a furnace condition sensor attached to the furnace body 8, 11 is an electrode based on information from the voltage detection circuit 5, current detection circuit 6 and furnace condition sensor 10. It is a control device for adjusting the lifting device 9, the variable reactance 4 and the furnace transformer 3, and the control device 11 includes a power amount calculation circuit 12, a charging ratio setting circuit as shown in FIG.
13, arc length calculation circuit 14 and inductance calculation circuit 15
It has.
上記のように構成した交流アーク炉により溶解制御を
行なう方法を第4図に示したフローチヤートに基いて説
明する。A method of controlling melting by the AC arc furnace configured as described above will be described based on the flow chart shown in FIG.
まず、投入電力量Pと力率cosθを決定し制御装置11
に設定し(ステツプ40)、所定の電圧、電流を各電極7
に供給して溶解を行なう。この電圧、電流を電圧検出回
路5及び電流検出回路6で検出し制御装置11の電力量演
算回路12に入力して各電極7に供給している電力量を検
出する(ステツプ41)。First, the input power amount P and the power factor cos θ are determined and the control device 11
(Step 40) and set the specified voltage and current to each electrode 7.
To dissolve it. The voltage and current are detected by the voltage detection circuit 5 and the current detection circuit 6 and input to the power amount calculation circuit 12 of the control device 11 to detect the amount of power supplied to each electrode 7 (step 41).
次に溶解の進捗にともない炉況センサ10で溶解の進捗
不均一性を検出し(ステツプ42)、進捗不均一性にした
がつて投入比率設定回路13に各相への必要な投入比率を
設定する(ステツプ43)。この各相の投入比率と電力量
演算回路12で演算した各相の投入電力量によりアーク長
演算回路14で電流I一定の条件で各相のアーク長を演算
決定し(ステツプ44)、決定したアーク長になるように
電極昇降装置9を駆動する(ステツプ45)。一方、アー
ク長演算回路14で演算した各相のアーク長に基づき各相
の可変リアクトル4のインダクタンスをインダクタンス
演算回路15で演算し(ステツプ46)、各相の可変リアク
トル4のタツプを切換え(ステツプ47)、溶解を進める
(ステツプ48)ことにより溶解が均一になるように制御
を行なう。Next, along with the progress of melting, the furnace condition sensor 10 detects the non-uniformity of the progress of melting (step 42), and according to the non-uniformity of progress, sets the necessary ratio of charging to each phase in the charging ratio setting circuit 13. Yes (step 43). The arc length calculation circuit 14 calculates and determines the arc length of each phase under the condition that the current I is constant based on the input ratio of each phase and the input power amount of each phase calculated by the electric energy calculation circuit 12 (step 44). The electrode elevating device 9 is driven so that the arc length is reached (step 45). On the other hand, based on the arc length of each phase calculated by the arc length calculation circuit 14, the inductance of the variable reactor 4 of each phase is calculated by the inductance calculation circuit 15 (step 46), and the tap of the variable reactor 4 of each phase is switched (step 47) Then, control is performed so that the dissolution becomes uniform by advancing the dissolution (step 48).
なお、上記実施例において、常に溶解の早い相や遅い
相が明らかに決まつている場合には第5図に示すように
各相に応じてあらかじめベースとなる固定容量を想定し
て固定リアクトル4a,4bを付加しておき、平均的な均等
溶解ができるようにしておいた後に、炉の各チヤージ毎
にスクラツプの入りかたや酸素の吹きかたなどによつて
溶解が不均一になる部分を各相に設けた可変リアクトル
4で制御しても良い。In the above-mentioned embodiment, when it is clear that the fast-dissolving phase or the slow-dissolving phase is always decided, the fixed reactor 4a is assumed by assuming a fixed capacity as a base in advance according to each phase as shown in FIG. , 4b have been added to enable uniform uniform melting, and then the areas where the melting becomes uneven due to the way the scrap is inserted and the way oxygen is blown for each charge in the furnace. You may control by the variable reactor 4 provided in the phase.
この発明は以上説明したように、三相交流の各相に設
けた可変リアクトルを調整することにより各相に流れる
電流の平衡を保ちながら各相の投入電力を調整するか
ら、電源に対して不平衡電流を流さずに各相の投入電力
バランスをより巾広く調整でき均等溶解を行なうことが
できる。As described above, the present invention adjusts the input power of each phase while maintaining the balance of the currents flowing in each phase by adjusting the variable reactors provided in each phase of the three-phase alternating current. It is possible to adjust the input power balance of each phase more broadly without flowing an equilibrium current and to perform uniform melting.
また、各相の電流は同じでアーク電圧のみが変わるの
で、溶け残り防止をねらう時のようなロングアーク効果
をもたせるのに有効であり、かつその効果の推定が電流
を調整する場合と異なり容易となる。In addition, the current of each phase is the same and only the arc voltage changes, so it is effective to have a long arc effect such as when aiming to prevent unmelted residue, and the estimation of that effect is easy, unlike when adjusting the current. Becomes
さらに三相の全リアクタンスの増減によつて、ロング
アークを形成するのに必要な高リアクタンスあるいはシ
ヨートアークを形成するときに有効な低リアクタンスの
両者の選択が可能となり、常にアークを安定させ、かつ
炉況に応じた熱バランスを設定できる効果を有する。Furthermore, by increasing / decreasing the total reactance of the three phases, it becomes possible to select both high reactance necessary for forming a long arc and low reactance effective in forming a short arc. It has the effect of setting the heat balance according to the situation.
第1図はこの発明の実施例を示す回路図、第2図は第1
図に示した実施例の交流アーク炉の構成図、第3図は上
記実施例の制御装置のブロツク図、第4図は上記実施例
の動作を示すフローチヤート、第5図は他の実施例のリ
アクトルを示す回路図である。 3…炉用変圧器、4…可変リアクトル、5…電圧検出回
路、6…電流検出回路、7…電極、9…電極昇降装置、
10…炉況センサ、11…制御装置。FIG. 1 is a circuit diagram showing an embodiment of the present invention, and FIG.
FIG. 3 is a block diagram of the AC arc furnace of the embodiment shown in the figure, FIG. 3 is a block diagram of the controller of the above embodiment, FIG. 4 is a flow chart showing the operation of the above embodiment, and FIG. 5 is another embodiment. 3 is a circuit diagram showing a reactor of FIG. 3 ... Transformer for reactor, 4 ... Variable reactor, 5 ... Voltage detection circuit, 6 ... Current detection circuit, 7 ... Electrode, 9 ... Electrode lifting device,
10 ... Reactor condition sensor, 11 ... Control device.
フロントページの続き (56)参考文献 特開 昭53−43254(JP,A) 実開 昭48−61441(JP,U) 実開 昭62−47097(JP,U) 実開 昭57−52096(JP,U) 実開 昭59−163895(JP,U) 特公 昭48−11538(JP,B1) 特公 昭55−17314(JP,B2) 実公 昭44−7210(JP,Y1)Continuation of the front page (56) References JP-A-53-43254 (JP, A) Actual opening 48-61441 (JP, U) Actual opening 62-47097 (JP, U) Actual opening 57-52096 (JP , U) Actual Development Sho 59-163895 (JP, U) Japanese Patent Sho 48-11538 (JP, B1) Japanese Official Sho 55-17314 (JP, B2) Actual Sho 44-7210 (JP, Y1)
Claims (4)
して電極のアーク長を変化させて溶解を促進するとき、
特定の自己インダクタンス及び相互インダクタンスを有
する給電回路の各相に個別に設けた調整可能な可変リア
クトルによって、給電回路の各相から各電極に流れる電
流を一定にしながら各相の電極に必要とする投入電力量
に応じて上記可変リアクトルを調整することを特徴とす
る交流アーク炉の溶解制御法。1. When facilitating melting by changing the arc length of an electrode in response to a change in melting rate of a three-phase AC arc furnace,
Adjustable variable reactors provided individually for each phase of the power supply circuit that have specific self-inductance and mutual inductance make the required currents for each phase electrode while keeping the current flowing from each phase of the power supply circuit to each electrode constant. A melting control method for an AC arc furnace, which comprises adjusting the variable reactor according to the amount of electric power.
することを特徴とする特許請求の範囲第1項記載の交流
アーク炉の溶解制御法。2. The melting control method for an AC arc furnace according to claim 1, wherein the power factor cos θ of the power supply circuit is set to 0.9 or less.
を設けて溶解の遅いまたは早い特性を有する相をなくす
るように溶解速度を平均化した三相交流アーク炉の溶解
速度の変化に対応して電極のアーク長を変化させて溶解
を促進するとき、特定の自己インダクタンス及び相互イ
ンダクタンスを有する給電回路の各相から各電極に流れ
る電流を一定にするように給電回路各相に個別に設けた
調整可能な可変リアクトルによって、各相の電極に必要
とする投入電力量に応じて上記可変リアクトルを調整す
ることを特徴とする交流アーク炉の溶解制御法。3. A change in melting rate of a three-phase AC arc furnace in which a fixed reactor is provided in one or more phases of each of the power feeding circuits and the melting rates are averaged so as to eliminate phases having slow or fast melting characteristics. When the arc length of the electrodes is changed correspondingly to promote melting, the current flowing from each phase of the power supply circuit, which has a specific self-inductance and mutual inductance, to each electrode is made constant so that the current flows to each electrode individually. A melting control method for an AC arc furnace, characterized in that the adjustable reactor provided is adjusted to adjust the variable reactor according to the amount of electric power input to the electrodes of each phase.
することを特徴とする特許請求の範囲第第3項記載の交
流アーク炉の溶解制御法。4. The melting control method for an AC arc furnace according to claim 3, wherein the power factor cos θ of the power supply circuit is set to 0.9 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61195632A JP2526554B2 (en) | 1986-08-22 | 1986-08-22 | Dissolution control method for AC arc furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61195632A JP2526554B2 (en) | 1986-08-22 | 1986-08-22 | Dissolution control method for AC arc furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6353891A JPS6353891A (en) | 1988-03-08 |
| JP2526554B2 true JP2526554B2 (en) | 1996-08-21 |
Family
ID=16344391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61195632A Expired - Lifetime JP2526554B2 (en) | 1986-08-22 | 1986-08-22 | Dissolution control method for AC arc furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2526554B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS447210Y1 (en) * | 1966-05-21 | 1969-03-18 | ||
| JPS4861441U (en) * | 1971-11-11 | 1973-08-04 |
-
1986
- 1986-08-22 JP JP61195632A patent/JP2526554B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6353891A (en) | 1988-03-08 |
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