JPH0711393B2 - Burner blowout detection method for smelting electric furnace - Google Patents
Burner blowout detection method for smelting electric furnaceInfo
- Publication number
- JPH0711393B2 JPH0711393B2 JP27380789A JP27380789A JPH0711393B2 JP H0711393 B2 JPH0711393 B2 JP H0711393B2 JP 27380789 A JP27380789 A JP 27380789A JP 27380789 A JP27380789 A JP 27380789A JP H0711393 B2 JPH0711393 B2 JP H0711393B2
- Authority
- JP
- Japan
- Prior art keywords
- burner
- blow
- vibration
- raw material
- electric 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 - Lifetime
Links
- 238000003723 Smelting Methods 0.000 title claims description 6
- 238000001514 detection method Methods 0.000 title description 5
- 239000002994 raw material Substances 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 239000000567 combustion gas Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000002893 slag Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 230000002411 adverse Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229910000863 Ferronickel Inorganic materials 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は燃料と酸素もしくは酸素富化空気等の酸素含有
気体とをバーナーを用いて、製錬用電気炉の原料層中で
燃焼させ、火炎および燃焼ガスにて原料を加熱、溶解す
るようにした電気炉において、バーナーの吹抜けを検知
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention uses a burner to burn fuel and oxygen or an oxygen-containing gas such as oxygen-enriched air in a raw material layer of an electric furnace for smelting, The present invention relates to a method for detecting blower blow-through in an electric furnace in which a raw material is heated and melted by a flame and a combustion gas.
(従来の技術) 従来、例えばフエロニッケルの製錬用電気炉では第1図
に示すように、電気炉2に800〜900℃に予熱された粉粒
状の原料3を投原管4から装入し3本の電極5に通電
し、主としてスラグ層6を介して電極5間に流れる数万
アンペアの大電流によるジュール熱によって原料3を加
熱溶解させる。その際、原料3中の鉱石と還元剤とが反
応して溶体として沈降し、比重差によりスラグ層6とメ
タル層7が形成される。一方、原料3は投原管4からチ
ヨークフィードされているので、溶解されて容積が減少
すると逐次炉内に流入する。そして、所定時間毎にスラ
グとメタルが抜き取られるようになっている。(Prior Art) Conventionally, for example, in an electric furnace for smelting ferro-nickel, as shown in FIG. 1, an electric furnace 2 is charged with a granular material 3 preheated to 800 to 900 ° C. from a throwing tube 4. Then, the three electrodes 5 are energized, and the raw material 3 is heated and melted by Joule heat due to a large current of tens of thousands amperes flowing between the electrodes 5 mainly through the slag layer 6. At that time, the ore in the raw material 3 reacts with the reducing agent to settle as a solution, and the slag layer 6 and the metal layer 7 are formed due to the difference in specific gravity. On the other hand, since the raw material 3 is fed from the throwing tube 4 by the yoke yoke, when the raw material 3 is melted and its volume decreases, the raw material 3 successively flows into the furnace. Then, the slag and the metal are extracted every predetermined time.
ところで、我国では電気エネルギーが高価な為安価な化
石燃料を使用して電気エネルギーの一部を代替する技術
が開発されつつある。その一環として電気炉内の原料3
の層の高温部にバーナー1を挿入してバーナー1の先端
で、重油又は微粉炭を酸素又は酸素含有空気で燃焼さ
せ、原料3の溶解を促進する方法がある。この方法では
第1図のように、長さ5〜6mの細長いバーナー1を複数
本、夫々炉外でガイド10によってスライド可能に支承
し、炉蓋8に設けた孔から原料3の中へ斜め上方から挿
入して、スラグ層6の上方の原料3の高温部で燃料を燃
焼させるようになっている。このようにすると、電気エ
ネルギーと高温の火炎と燃焼ガスによって原料3は溶解
されて溶体となり、スラグ層6に滴下してメタルとスラ
グに分離されメタルはメタル層7に沈降する。By the way, since electric energy is expensive in Japan, a technique for replacing a part of electric energy by using an inexpensive fossil fuel is being developed. As a part of that, raw material 3 in the electric furnace
There is a method of inserting the burner 1 into the high temperature part of the layer and burning the heavy oil or pulverized coal with oxygen or oxygen-containing air at the tip of the burner 1 to promote the dissolution of the raw material 3. In this method, as shown in FIG. 1, a plurality of slender burners 1 having a length of 5 to 6 m are slidably supported by guides 10 outside the furnace, respectively, and slanted into a raw material 3 through holes provided in a furnace lid 8. The fuel is burned in the high temperature part of the raw material 3 above the slag layer 6 by inserting from above. By doing so, the raw material 3 is melted into a solution by electric energy, high-temperature flame and combustion gas, drops into the slag layer 6, is separated into metal and slag, and the metal is deposited in the metal layer 7.
一方、各バーナー1の先端部で発生した高温ガスは、粉
粒状の原料3の空隙部を通過して原料3を予熱しながら
上昇して、原料3の表面全体から炉蓋8に設けられた煙
道9を通って排出され、鉱石や副原料の乾燥、予熱等に
再利用される。On the other hand, the high-temperature gas generated at the tip of each burner 1 passes through the voids of the powdery raw material 3 and rises while preheating the raw material 3, and is provided on the furnace lid 8 from the entire surface of the raw material 3. It is discharged through the flue 9 and is reused for drying ore and ore and ore materials.
(本発明が解決しようとする課題) 上記した方法において、最も効率よく原料を加熱するた
めには、バーナー1の先端部で発生した高温の燃焼ガス
が広い範囲の原料3と接触しつつ原料層内の空隙を上昇
することが望ましい。しかしながら、燃焼ガスが一ヶ所
だけから噴出する状態が発生する場合がある。この場
合、燃焼ガスは狭い範囲の原料だけを加熱し、又はほと
んど原料と接触しないで、高温のまま原料層から放出さ
れることになり、熱効率が悪くなる。そして数分間経過
後には一部の加熱された原料中の鉱石が溶解し、燃焼ガ
スとともに噴出する吹抜けと言われる状態を発生する。
この吹抜け発生時に噴出される溶解鉱石は時間の経過と
ともに多くなり、前記した如く熱効率が悪化するのみな
らず、電気炉の炉蓋8への局部的な加熱や溶解鉱石の付
着等を惹起する。また、投原管4の下部に溶解鉱石が付
着し投原管4を詰らせる等、種々の電気炉への悪影響を
およぼす結果となる。また、バーナー1に溶解鉱石が付
着、凝固しバーナー操作を困難にするのみならず、最悪
の場合にはバーナーやバーナー先端のノズルを溶損する
などの事態が発生する。且つ原料層内に筒状に溶解鉱石
が凝固して所謂煙道を形成し、一旦バーナーの吹込燃焼
操作を中止した後、再度バーナーの吹込燃焼を再開して
も容易に吹抜けが再発する原因となる。(Problems to be Solved by the Invention) In the above method, in order to heat the raw material most efficiently, the high temperature combustion gas generated at the tip of the burner 1 is in contact with a wide range of the raw material 3 and the raw material layer. It is desirable to raise the voids inside. However, there is a case where the combustion gas is ejected from only one place. In this case, the combustion gas heats only the raw material in a narrow range or hardly contacts the raw material, and is discharged from the raw material layer at a high temperature, resulting in poor thermal efficiency. After a few minutes, some ore in the heated raw material is melted, and a state called blow-by blows out together with the combustion gas.
The molten ore ejected at the time of occurrence of the blow-through increases with time, and not only the thermal efficiency deteriorates as described above, but also local heating to the furnace lid 8 of the electric furnace and adhesion of the molten ore occur. In addition, the molten ore adheres to the lower part of the throwing tube 4 and clogs the throwing tube 4, resulting in adverse effects on various electric furnaces. Further, not only the molten ore adheres to the burner 1 and solidifies to make the burner operation difficult, but in the worst case, the burner and the nozzle at the tip of the burner are melted and damaged. In addition, the molten ore solidifies in a tubular shape in the raw material layer to form a so-called flue, and once the blower combustion operation of the burner has been stopped, the blow-through easily reoccurs even if the burner injection combustion is restarted. Become.
したがって、吹抜けが発生した場合は、早期にバーナー
を原料層から引き抜き、角度を変更して再挿入し吹抜け
の解消をはかるとか、一旦吹込燃焼を中止し炉況の回復
を待つ等の操作が必要である。Therefore, if blow-through occurs, it is necessary to remove the burner from the raw material layer at an early stage, reinsert it by changing the angle to eliminate the blow-through, or stop the blow-in combustion once and wait for the recovery of the furnace condition. Is.
しかしながら従来、吹抜けが発生したことを発見するの
が困難であるという問題点があった。またそのため、吹
抜け発生を発見するために作業者が頻繁に炉内の点検を
行なわねばならず、作業員の負担が大きいという問題点
もあった。However, conventionally, there has been a problem that it is difficult to detect that a blow-through has occurred. Therefore, the worker must frequently inspect the inside of the furnace in order to detect the occurrence of blow-through, which causes a problem that the burden on the worker is large.
本発明は上記の問題点を解消し、吹抜け状態を早期に、
且つ確実に発見することを課題とする。The present invention solves the above-mentioned problems, and makes the blow-through state early.
And the task is to make sure to discover it.
(課題を解決するための手段) 上記の課題を解決するために本発明は、炉内に挿入した
バーナーに燃料と酸素含有気体を供給し、炉内の原料中
でバーナーを燃焼せしめるようにした電気炉において、
バーナーの振動を振動センサーを介して検出し、その振
動の強さが一定レベル以上となったときを検知すること
を特徴とする製錬用電気炉のバーナー吹抜検知方法にあ
る。(Means for Solving the Problems) In order to solve the above problems, the present invention supplies a fuel and an oxygen-containing gas to a burner inserted in a furnace, and burns the burner in a raw material in the furnace. In the electric furnace,
A burner blowout detection method for an electric furnace for smelting is characterized by detecting vibration of a burner through a vibration sensor and detecting when the vibration intensity exceeds a certain level.
第1図に、本発明方法を実施するための装置の一例を示
す。ガイド10の上端に振動センサー11を設け、この振動
の強さの信号は増幅器12で増幅した後、バンドパスフィ
ルター13で10dB以上の周波数だけを抽出し、モニター14
に表示するとともに判別回路15に入り、ここで通常操作
時の振動の強さと比較し、警報器16を作動させるように
構成されている。なお、必要に応じてバーナー1の駆動
装置に連動させてバーナー1を自動的に引上げるように
構成することもできる。FIG. 1 shows an example of an apparatus for carrying out the method of the present invention. A vibration sensor 11 is provided at the upper end of the guide 10, and a signal of this vibration intensity is amplified by an amplifier 12 and then a bandpass filter 13 extracts only a frequency of 10 dB or more.
It is configured to activate the alarm 16 by comparing with the strength of vibration during normal operation. Note that the burner 1 can be automatically pulled up by interlocking with the drive device of the burner 1 if necessary.
(作用) 上記した本発明の方法によれば、振動センサー11によっ
て検出されるバーナー1の振動は、吹抜けを発生してな
い正常な状態のときと吹抜けを発生している状態とで振
動の強さが異なるので、吹抜けの発生を容易に検知でき
るという作用を為す。(Operation) According to the above-described method of the present invention, the vibration of the burner 1 detected by the vibration sensor 11 has a strong vibration in a normal state in which no blow-through occurs and in a state in which blow-through occurs. Since the difference is different, it has an effect that the occurrence of blow-by can be easily detected.
(実施例) 実施例1 第2図の部分拡大図に示すように、ガイド10の上端部に
二ケの振動センサー11a,11bをそれぞれ取付アーム17,18
に取付け、バーナー1の縦方向の振動(第2図の矢印A
で示す)を振動センサー11aにより、また横方向の振動
(第2図の矢印Bで示す)を振動センサー11bにより検
出するように配設し、バーナー1より燃料と酸素を原料
層に吹込んで燃焼させながら電気炉の操業を行なった。
操業中に測定した10kHz以下の周波数の振動の強さを表
1及び表2に示す。表1は縦方向振動の吹抜け前30分間
の振動の強さイと吹抜け中の振動の強さロの対比であ
る。表2は横方向振動についての吹抜け前30分間の振動
の強さハと吹抜け中の振動の強さニの対比である。な
お、吹抜けの有無の確認は警報作動時、及び記録した振
動の強さが大きくなりつつある時等を参考に目視により
行なった。(Embodiment) Embodiment 1 As shown in a partially enlarged view of FIG. 2, two vibration sensors 11a and 11b are attached to the upper end of the guide 10 by mounting arms 17 and 18, respectively.
Attached to the vertical axis of the burner 1 (arrow A in FIG. 2).
Is indicated by a vibration sensor 11a, and lateral vibration (indicated by an arrow B in FIG. 2) is detected by a vibration sensor 11b. The burner 1 blows fuel and oxygen into the raw material layer for combustion. While operating the electric furnace.
Tables 1 and 2 show the vibration intensities of frequencies below 10 kHz measured during operation. Table 1 shows a comparison between the vibration intensity a during the 30 minutes before the vertical vibration blow through and the vibration intensity b during the blow through. Table 2 shows a comparison of the vibration intensity c during the 30 minutes before the blow-through and the vibration intensity d during the blow-through for the lateral vibration. The presence / absence of blow-through was visually confirmed at the time of alarm activation and when the recorded vibration intensity was increasing.
表1の縦方向振動の吹抜け前の30〜20分、20〜10分、10
〜0分の各振動の強さの平均は各々、6.46dB,6.34dB,
6.89dBと略同一であり、全平均は6.62dBであった。これ
に対して吹抜け発生中の振動の強さの平均は14.3dBで
あり、吹抜け発生中の方が7.68dB強くなっている。又、
吹抜け中の振動ピーク値の平均である18.31dBとの比
較では11.89dB強くなっていた。次に表2の横方向振動
を同様に比べると、吹抜け前の各は16.00dB,16.14dB,
17.65dBで全平均は16.64dBである。これに対し、吹抜け
発生中の振動のは25.33dBで8.69dB強くなっており吹
抜け発生中の振動ピーク値の平均28.54dBとの比較で
は11.90dB強くなっていることが判った。次に縦、横両
方向の振動について、吹抜け発生前10分間と吹抜け発生
中の2つの振動の強さの母平均の差に関する検定を行な
ったところ、有意水準1%で高度に有意差があると言え
ることが判った。30 to 20 minutes, 20 to 10 minutes before blow-through of longitudinal vibration in Table 1, 10
The average of each vibration intensity for 0 min is 6.46dB, 6.34dB,
It was almost the same as 6.89 dB, and the total average was 6.62 dB. On the other hand, the average vibration intensity during blow-through is 14.3 dB, which is 7.68 dB stronger during blow-through. or,
It was 11.89 dB stronger than 18.31 dB, which is the average of the vibration peak values during the void. Next, comparing the lateral vibrations of Table 2 in the same way, it was 16.00dB, 16.14dB,
At 17.65 dB, the overall average is 16.64 dB. On the other hand, it was found that the vibration during blow-through was 25.33 dB, which was 8.69 dB stronger, and was 11.90 dB stronger than the average vibration peak value during blow-through, which was 28.54 dB. Next, for the vibrations in both the vertical and horizontal directions, we tested the difference between the population mean of the vibration intensity for 10 minutes before the occurrence of the blowout and the vibration intensity during the occurrence of the blowout and found that there was a highly significant difference at the significance level of 1%. I understood that I can say.
実施例2 実施例1と同じ電気炉で、同様の装置を用いて、振動の
強さの分散が小さく、吹抜け発生前と吹抜け発生中の振
動の強さのレベル差が判別し易いバーナー縦方向の振動
について7dB以上の差があれば警報を作動させるように
して、吹抜けの発生と警報の有無の関係を調べた。ここ
で 正報(吹抜け発生中であり、警報も作動した)回数 誤報(吹抜けは発生していないが警報が作動した)回
数 未検知(吹抜け発生中であるが警報が作動しない)回
数 検知率(%)={/(+)}×100 正報率(%)={/(+)}×100 としたところ検知率は約70%、正報率は約60%であっ
た。の誤報の原因は瞬間的に7dB以上の振動の強さの
差があったこと、の未検知の原因は吹抜け発生中の振
動の強さの差が7dB以下であったこと等があるが、振動
センサーの取付位置等を工夫することで、検知率、正報
率ともより改善可能な見通しが得られた。Example 2 A burner longitudinal direction in which the same electric furnace as in Example 1 was used and the same apparatus was used, the dispersion of vibration intensity was small, and the level difference in vibration intensity before and during blow-through was easy to distinguish. The alarm was activated if there was a difference of 7 dB or more with respect to the vibration, and the relationship between the occurrence of blow-by and the presence or absence of the alarm was investigated. Here, the number of correct reports (there was a blowout and the alarm was activated), the number of false reports (there was no blowout, but the alarm was activated) the number of undetected (the blowout was generated but the alarm did not activate) detection rate ( %) = {/ (+)} × 100 Correct reporting rate (%) = {/ (+)} × 100 The detection rate was about 70% and the correct reporting rate was about 60%. The cause of the false alarm was that there was a momentary difference in vibration intensity of 7 dB or more, and the cause of undetected was that the difference in vibration intensity during the occurrence of blow-through was 7 dB or less. By improving the mounting position of the vibration sensor, it was possible to improve the detection rate and the accuracy rate.
(本発明の効果) 以上詳細に説明したように、本発明によれば、製錬用電
気炉のバーナーに吹抜けが発生すれば自動的に検知でき
るので、吹抜けの状態を発見するのが遅れたことによる
電気炉への悪影響やバーナー、ノズルの損傷等を防止で
き、吹込燃焼の稼働率を向上できるという効果がある。
さらに、作業員が直接炉内を監視することなく、遠隔
(例えば警報設置した操作室内)にて吹抜け発生を知り
得るので、作業員の負坦を軽減することができるという
効果もある。 (Effect of the present invention) As described in detail above, according to the present invention, if a blow-through occurs in the burner of the smelting electric furnace, it can be automatically detected, so that the state of blow-through has been delayed. This has the effect of preventing adverse effects on the electric furnace, damage to the burner and nozzle, etc., and improving the operating rate of blow-in combustion.
Further, since the worker can know the occurrence of blow-through remotely (for example, in the operation room where an alarm is installed) without directly monitoring the inside of the furnace, there is an effect that the burden on the worker can be reduced.
第1図は本発明方法を実施するための装置の一例を示す
図、第2図は本発明を実施する装置の振動センサーの取
付部を示す部分拡大図である。 1……バーナー、2……電気炉、3……原料、10……ガ
イド、11……振動センサー。FIG. 1 is a view showing an example of an apparatus for carrying out the method of the present invention, and FIG. 2 is a partially enlarged view showing a mounting portion of a vibration sensor of the apparatus for carrying out the present invention. 1 ... Burner, 2 ... Electric furnace, 3 ... Raw material, 10 ... Guide, 11 ... Vibration sensor.
Claims (1)
気体を供給し、炉内の原料中でバーナーを燃焼せしめる
ようにした電気炉において、バーナーの振動を振動セン
サーを介して検出し、その振動の強さが一定レベル以上
となったときを検知することを特徴とする製錬用電気炉
のバーナー吹抜検知方法。1. An electric furnace in which a fuel and an oxygen-containing gas are supplied to a burner inserted in a furnace to burn the burner in a raw material in the furnace, the vibration of the burner is detected through a vibration sensor, A method for detecting burner blow-out in an electric furnace for smelting, which detects when the intensity of vibration exceeds a certain level.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27380789A JPH0711393B2 (en) | 1989-10-23 | 1989-10-23 | Burner blowout detection method for smelting electric furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27380789A JPH0711393B2 (en) | 1989-10-23 | 1989-10-23 | Burner blowout detection method for smelting electric furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03137488A JPH03137488A (en) | 1991-06-12 |
| JPH0711393B2 true JPH0711393B2 (en) | 1995-02-08 |
Family
ID=17532842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27380789A Expired - Lifetime JPH0711393B2 (en) | 1989-10-23 | 1989-10-23 | Burner blowout detection method for smelting electric furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0711393B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4770478B2 (en) * | 2005-04-01 | 2011-09-14 | 株式会社デンソー | Air quality component supply device for vehicles |
-
1989
- 1989-10-23 JP JP27380789A patent/JPH0711393B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03137488A (en) | 1991-06-12 |
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