JPH04272117A - Method for detecting bridging in melting scrap - Google Patents
Method for detecting bridging in melting scrapInfo
- Publication number
- JPH04272117A JPH04272117A JP3030059A JP3005991A JPH04272117A JP H04272117 A JPH04272117 A JP H04272117A JP 3030059 A JP3030059 A JP 3030059A JP 3005991 A JP3005991 A JP 3005991A JP H04272117 A JPH04272117 A JP H04272117A
- Authority
- JP
- Japan
- Prior art keywords
- scrap
- converter
- oxygen
- melting
- shelf
- 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.)
- Pending
Links
- 238000002844 melting Methods 0.000 title claims abstract description 22
- 230000008018 melting Effects 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000001301 oxygen Substances 0.000 claims abstract description 25
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 25
- 238000002485 combustion reaction Methods 0.000 claims abstract description 9
- 238000007664 blowing Methods 0.000 claims description 18
- 239000007789 gas Substances 0.000 claims description 17
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000007670 refining Methods 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 description 9
- 239000010959 steel Substances 0.000 description 9
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 239000003575 carbonaceous material Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 101000582320 Homo sapiens Neurogenic differentiation factor 6 Proteins 0.000 description 1
- 102100030589 Neurogenic differentiation factor 6 Human genes 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000005262 decarbonization Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
- 239000002918 waste heat Substances 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
- Y02P10/20—Recycling
Landscapes
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、転炉等において酸素吹
込みによるスクラップの溶解・精錬時に発生するいわゆ
る″棚吊り″を検知する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for detecting so-called "shelf hanging" that occurs during melting and refining of scrap by oxygen injection in a converter or the like.
【0002】0002
【従来の技術】近年、価格的に有利なことから、製鋼材
料に占めるスクラップの割合が増加の傾向にある。従来
より、スクラップの溶解に際しては、電気炉による場合
がほとんどであったが、電気料金が嵩むことから、その
溶解熱源を電力では無しに、炭材による大量の熱量を供
給できる転炉設備によるスクラップの溶解技術が注目さ
れるようになってきた。BACKGROUND OF THE INVENTION In recent years, the proportion of scrap in steelmaking materials has been increasing due to its advantageous price. Traditionally, scrap has been melted in most cases using electric furnaces, but due to the high electricity costs, it is now possible to melt scrap using converter equipment, which can supply a large amount of heat from carbonaceous materials without using electricity as the heat source for melting. The dissolution technology of is now attracting attention.
【0003】従来よりの転炉におけるスクラップ溶解・
精錬方法としては、たとえば本出願人等が先の特願昭6
0−185192号公報に開示されたものがある。この
スクラップ溶解・精錬方法は、上・底両吹き複合吹錬転
炉に先ず50〜200kg/tのコークスを投入し、底
吹き羽口または上吹きランスの一方あるいは双方から酸
素ガスを吹き込んでコークスを着火させ火種とした後ス
クラップを装入し、さらに炭材を投入しながら底吹き羽
口および上吹きランスから酸素ガスを吹き込んで、製品
窒素量の低減のため溶解完了時の溶鋼中C量;2.0%
以上を確保し得るように溶解を進め、スクラップ溶解が
完了した後、塩基度(CaO/SiO2 )が1.2以
上となるようにスラグ成分を調整して脱硫を行うととも
に、底吹き羽口より非酸化性ガスを吹き込むことでスラ
グと溶鋼を攪拌してスラグ中の全Fe量の3%未満とし
、次いで脱硫完了後にスラグと残留炭材を除去してから
上・底吹き送酸することによって脱炭・脱窒するもので
ある。[0003] Conventional scrap melting in converter
As for the refining method, for example, the applicant et al.
There is one disclosed in Japanese Patent No. 0-185192. In this scrap melting and refining method, 50 to 200 kg/t of coke is first charged into a top- and bottom-blowing combined blowing converter, and oxygen gas is blown into the bottom-blowing tuyere or top-blowing lance, or both. After igniting it to create a spark, the scrap is charged, and while the carbon material is being added, oxygen gas is blown from the bottom blowing tuyere and top blowing lance to reduce the amount of carbon in the molten steel upon completion of melting to reduce the amount of nitrogen in the product. ;2.0%
Melting proceeds to ensure the above, and after scrap melting is completed, desulfurization is performed by adjusting the slag components so that the basicity (CaO/SiO2) is 1.2 or more, and the bottom blowing tuyere By blowing in non-oxidizing gas, the slag and molten steel are stirred to reduce the total amount of Fe in the slag to less than 3%, and then, after desulfurization is completed, the slag and residual carbonaceous material are removed, and then top and bottom blowing is carried out. It decarburizes and denitrifies.
【0004】0004
【発明が解決しようとする課題】前記転炉におけるスク
ラップ溶解・精錬方法においては、図3に示されるよう
に、酸素ランス13からのO2 ガスが直接的に衝突し
ない鋼浴12の周囲部分に炉壁10に拘束されて棚状に
未溶解のスクラップ11が付着する、いわゆる″棚吊り
″11と呼ばれる現象が発生する。この″棚吊り″11
は、一旦形成されると、投入したエネルギーの消費効率
を悪化させるため、エネルギー源であるコークスおよび
O2 ガスの消費量が増大するとともに、さらに進行し
た場合には操業が不能になるなどの問題を誘発する場合
があった。In the method for melting and refining scrap in a converter, as shown in FIG. A phenomenon called "shelf hanging" 11 occurs, in which unmelted scrap 11 is bound to the wall 10 and adheres in the form of a shelf. This “shelf hanging” 11
Once formed, it deteriorates the consumption efficiency of the input energy, increasing the consumption of coke and O2 gas, which are the energy sources, and if it progresses further, it can cause problems such as the inability to operate. There were cases where it was triggered.
【0005】さらに、前記″棚吊り″11が形成された
状態で、転炉を転倒させた場合、前記″棚吊り″11は
過酸化状態にあるため、この″棚吊り″11と大量の溶
鋼12との接触により異常反応を起こし危険であるとと
もに、転炉10の上方側に位置する″棚吊り″11の一
部が落下することにより溶鋼12のはね返りが生じ、周
囲にいる作業員が危険に晒されるなどの問題があった。
したがって、前期″棚吊り″を検知し、これを未然に除
去することが重要となるが、従来より、前記″棚吊り″
の発生を検知する好適な方法は無く、一旦送酸をストッ
プし、転炉を転倒させて目視により確認するなどの方法
により行っていた。Furthermore, when the converter is turned over with the "shelf hangings" 11 formed, since the "shelf hangings" 11 are in a peroxidized state, the "shelf hangings" 11 and a large amount of molten steel are Contact with the converter 12 causes an abnormal reaction, which is dangerous, and a part of the "shelf hanging" 11 located above the converter 10 falls, causing the molten steel 12 to bounce back, putting workers in the vicinity at risk. There were problems such as exposure to Therefore, it is important to detect the early "shelf hanging" and eliminate it before it occurs.
There is no suitable method for detecting the occurrence of oxidation, and conventional methods include temporarily stopping the oxygen supply, overturning the converter, and visually checking.
【0006】そこで、本発明の主たる目的は、作業の安
全およびエネルギー源の節減を図るべく、スクラップの
溶解に際しての″棚吊り″の発生の有無を、目視による
ことなく検知する方法を提供するものである。[0006] Therefore, the main object of the present invention is to provide a method for detecting the occurrence of "shelf hanging" during melting of scrap without visual inspection, in order to ensure work safety and save energy resources. It is.
【0007】[0007]
【課題を解決するための手段】前記課題は、反応容器内
のスクラップに対し酸素吹込みを行い溶解・精錬するに
当り、前記吹込み酸素の平均送酸速度を4 Nm3/m
in・t 以下として送給するとともに、逐次排ガスの
2次燃焼比率(%CO2 /(%CO+%CO2 ))
の測定を行い、100Nm3/t 送酸時の通算平均2
次燃焼比率が15%以下である場合に″棚吊り″発生有
りと判断することで解決できる。[Means for solving the problem] The problem is to increase the average oxygen supply rate of the blown oxygen to 4 Nm3/m when blowing oxygen into the scrap in the reaction vessel to melt and refine it.
in・t or less, and the secondary combustion ratio of exhaust gas (%CO2 / (%CO + %CO2 ))
Measurement was carried out, and the total average at 100Nm3/t oxygen supply was 2.
This problem can be solved by determining that "shelf hanging" has occurred when the subsequent combustion ratio is 15% or less.
【0008】[0008]
【作用】転炉などの反応容器内に収容されたスクラップ
に対して、酸素吹込みにより一定熱量を与え続けた場合
に、O2 ガスの衝突する所から徐々にスクラップの溶
融化が進む。その後、スクラップの溶融化しない部分が
炉壁の周囲に残り、いわゆる″棚吊り″として残存する
。
スクラップの溶融化が進んでいる内は、与熱量はスクラ
ップの溶融に使用されるため、鋼浴温度がある一定温度
に維持される。ところが、スクラップの溶融化が止まり
、″棚吊り″が形成し始めると、与熱量はスクラップの
溶融化には使用されずに溶鋼温度が上昇し始める。この
現象を溶鋼からの排ガスの関係で捉えると、CO2 +
C=2COの反応式が、″棚吊り″が形成され始めると
、鋼浴温度の上昇により、右側に進行し、排ガス組成中
のCO量が著しく多くなる。[Operation] When a constant amount of heat is continuously applied to the scrap stored in a reaction vessel such as a converter by oxygen injection, the scrap gradually melts from the point where the O2 gas collides with the scrap. Thereafter, the unmelted portion of the scrap remains around the furnace wall and remains as a so-called "hanging shelf." While the melting of the scrap is progressing, the heat input is used for melting the scrap, so the steel bath temperature is maintained at a certain constant temperature. However, when the melting of the scrap stops and "shelf hangings" begin to form, the heat input is not used to melt the scrap, and the temperature of the molten steel begins to rise. If we consider this phenomenon in terms of exhaust gas from molten steel, CO2 +
When the reaction equation of C=2CO begins to form a "shelf suspension", it progresses to the right due to the rise in steel bath temperature, and the amount of CO in the exhaust gas composition increases significantly.
【0009】本発明においては、この反応特性を利用し
、″棚吊り″を精度よく検知しようとするものである。
すなわち、″棚吊り″が形成され始めると、排ガス中の
CO量が増大するため、2次燃焼比率(%CO2 /(
%CO+%CO2 ))(以下、PC比率という)が著
しく減少することに着目し、このPC比率を測定するこ
とによって、″棚吊り″の有無を判断しようとするもの
である。酸素吹込みランスからの平均送酸速度を4 N
m3/min・t 以下とするのは、4 Nm3/mi
n・t を超えると、強攪拌となり2次燃焼が生じずに
優先脱Cするためである。また、PC比率を100Nm
3/t 送酸した時点での通算平均とするのは、100
Nm3/t を超えると、溶け落ちた溶銑の温度も上が
り、2次燃焼のベースが下がるためである。また、″棚
吊り″の有無の判断をPC比率15%以内とするのは、
本発明者等による試験結果に基づくものである。なお、
前記酸素吹込みが、上吹きと底吹きによる複合転炉であ
る場合には、平均送酸速度の合計値が4 Nm3/mi
n・t 以下であればよく、この際には底吹きO2 ガ
ス量が少なくとも0.5 Nm3/min・t 以上で
あることが望ましい。[0009] The present invention attempts to accurately detect "hanging on a shelf" by utilizing this reaction characteristic. In other words, when "shelf hanging" begins to form, the amount of CO in the exhaust gas increases, so the secondary combustion ratio (%CO2 / (
%CO+%CO2)) (hereinafter referred to as PC ratio) is significantly reduced, and by measuring this PC ratio, it is attempted to determine the presence or absence of "shelf hanging". The average oxygen delivery rate from the oxygen injection lance was set to 4 N.
m3/min・t or less is 4 Nm3/mi
This is because if it exceeds n·t, strong stirring will occur and preferential decarbonization will occur without secondary combustion occurring. Also, the PC ratio is 100Nm
3/t The total average at the time of oxygen delivery is 100
This is because if it exceeds Nm3/t, the temperature of the melted hot metal will also rise and the base of secondary combustion will fall. In addition, the judgment of the presence or absence of "shelf hanging" is based on the PC ratio of 15% or less.
This is based on test results by the inventors. In addition,
When the oxygen injection is a combined converter using top blowing and bottom blowing, the total value of the average oxygen feeding rate is 4 Nm3/mi.
n·t or less, and in this case, it is desirable that the bottom-blown O2 gas amount be at least 0.5 Nm3/min·t or more.
【0010】0010
【実施例】以下、本発明を実施例に基づき詳説する。図
1は、上・底吹き複合転炉におけるスクラップ溶解状況
を示す図であり、転炉1に装入されたスクラップ3は、
転炉1の上方に設備された酸素吹込みランス5からO2
ガスを吹き込むとともに、転炉1底からO2 ガスお
よびN2 ガスを吹き込んでスクラップ3の溶解が行わ
れる。
溶解によって発生する排ガスは、転炉1とフード4との
間の隙間から押し込まれるエアーにより燃焼され、図示
されな排熱ボイラによって蒸気として回収される。排ガ
ス中の%COおよび%CO2 の測定に際しては、実際
に酸素吹込みによるスクラップの溶解中に転炉内で%C
Oおよび%CO2 を連続分析することは、操業上の理
由により困難である。したがって、転炉1の上方の設置
されるフード4の煙道中で検出するのが望ましい。排ガ
ス中のCOガスは、転炉1炉口とフード4との隙間から
のエアーにより酸化されてCO2 ガスになるため、数
1に示される方法により、PC比率を求めるものとする
。EXAMPLES The present invention will be explained in detail below based on examples. FIG. 1 is a diagram showing the state of scrap melting in a top/bottom blowing combined converter, and the scrap 3 charged into the converter 1 is
O2 from the oxygen injection lance 5 installed above the converter 1
In addition to blowing in gas, O2 gas and N2 gas are also blown in from the bottom of the converter 1 to melt the scrap 3. Exhaust gas generated by melting is combusted by air forced into the gap between the converter 1 and the hood 4, and is recovered as steam by a waste heat boiler (not shown). When measuring %CO and %CO2 in exhaust gas, %CO2 is actually measured in the converter during melting of scrap by oxygen injection.
Continuous analysis of O and %CO2 is difficult due to operational reasons. Therefore, it is desirable to detect it in the flue of the hood 4 installed above the converter 1. Since the CO gas in the exhaust gas is oxidized by air from the gap between the opening of the converter 1 and the hood 4 to become CO2 gas, the PC ratio is determined by the method shown in Equation 1.
【0011】[0011]
【数1】[Math 1]
【0012】なお、上記式中における侵入Airは、窒
素バランスにより、具体的には数2より求めることがで
きる。Note that the intrusion Air in the above equation can be specifically determined from Equation 2 based on the nitrogen balance.
【0013】[0013]
【数2】[Math 2]
【0014】(実施例)前記転炉1において、酸素吹込
みランス5からの上吹き送酸速度を3.2 Nm3/m
in・t 、転炉底からの底吹き酸素速度を0.6 N
m3/min・t として、表1に示される成分のスク
ラップについて、HMR(溶銑率)=0%(全てスクラ
ップ)の下で、溶解・精錬を行い、100Nm3/t
送酸時点でのPC比率と″棚吊り″発生の有無との関係
について調査を行い、その試験結果を図2に示す。(Example) In the converter 1, the top blowing oxygen rate from the oxygen blowing lance 5 was set to 3.2 Nm3/m.
in・t, the bottom blowing oxygen rate from the bottom of the converter is 0.6 N.
m3/min・t, melting and refining the scrap with the components shown in Table 1 under HMR (hot metal ratio) = 0% (all scrap), 100Nm3/t
The relationship between the PC ratio at the time of oxygen supply and the occurrence of "shelf hanging" was investigated, and the test results are shown in Figure 2.
【0015】[0015]
【表1】[Table 1]
【0016】図2より明らかとなるように、PC率が1
5%以下の場合には、″棚吊り″の発生が見られるが、
15%を超える場合には″棚吊り″現象が見られず、P
C比率15%を境として、″棚吊り″の有無を判断でき
ることが判明される。As is clear from FIG. 2, when the PC rate is 1
If it is less than 5%, "shelf hanging" will occur,
If it exceeds 15%, no "shelf hanging" phenomenon is observed, and P
It is found that the presence or absence of "shelf hanging" can be determined at a C ratio of 15%.
【0017】[0017]
【発明の効果】以上小説のとおり、本発明によれば、転
炉を転倒せずとも簡単に″棚吊り″の発生の有無を確認
できるため、作業の安全が図れるとともに、その発生を
確実に把握できるため、適宜これを取り除くことによっ
て供給熱源の節減を図ることができる。[Effects of the Invention] As described in the novel above, according to the present invention, it is possible to easily check whether "shelf hanging" has occurred without overturning the converter, thereby ensuring work safety and ensuring that its occurrence is Since it can be grasped, it is possible to save the supply heat source by removing it as appropriate.
【図1】本発明に係る転炉におけるスクラップ溶解状況
図である。FIG. 1 is a diagram showing the state of scrap melting in a converter according to the present invention.
【図2】本実施例における試験結果を示す図である。FIG. 2 is a diagram showing test results in this example.
【図3】転炉におけるスクラップ溶解時の″棚吊り″発
生状況説明図である。FIG. 3 is an explanatory diagram of the occurrence of "shelf hanging" during scrap melting in a converter.
1 転炉 2 溶鋼 3 スクラップ 4 フード 5 酸素吹込みランス 1 Converter 2 Molten steel 3 Scrap 4 Food 5 Oxygen injection lance
Claims (1)
を行い溶解・精錬するに当り、前記吹込み酸素の平均送
酸速度を4 Nm3/min・t 以下として送給する
とともに、逐次排ガスの2次燃焼比率(%CO2 /(
%CO+%CO2 ))の測定を行い、100Nm3/
t 送酸時の通算平均2次燃焼比率が15%以下である
場合に″棚吊り″発生有りと判断することを特徴とする
スクラップ溶解における″棚吊り″検知方法。Claim 1: When blowing oxygen into scrap in a reaction vessel for melting and refining, the blown oxygen is fed at an average rate of 4 Nm3/min·t or less, and the exhaust gas is sequentially fed. Secondary combustion ratio (%CO2 / (
%CO+%CO2)) was measured and 100Nm3/
t. A method for detecting "shelf hanging" in scrap melting, characterized in that it is determined that "shelf hanging" has occurred when the total average secondary combustion ratio during oxygen supply is 15% or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3030059A JPH04272117A (en) | 1991-02-25 | 1991-02-25 | Method for detecting bridging in melting scrap |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3030059A JPH04272117A (en) | 1991-02-25 | 1991-02-25 | Method for detecting bridging in melting scrap |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04272117A true JPH04272117A (en) | 1992-09-28 |
Family
ID=12293258
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3030059A Pending JPH04272117A (en) | 1991-02-25 | 1991-02-25 | Method for detecting bridging in melting scrap |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04272117A (en) |
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1991
- 1991-02-25 JP JP3030059A patent/JPH04272117A/en active Pending
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