JPS61163204A - Converter blowing method - Google Patents
Converter blowing methodInfo
- Publication number
- JPS61163204A JPS61163204A JP211785A JP211785A JPS61163204A JP S61163204 A JPS61163204 A JP S61163204A JP 211785 A JP211785 A JP 211785A JP 211785 A JP211785 A JP 211785A JP S61163204 A JPS61163204 A JP S61163204A
- Authority
- JP
- Japan
- Prior art keywords
- converter
- dust
- iron
- blowing
- wet
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/30—Regulating or controlling the blowing
- C21C5/35—Blowing from above and through the bath
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/36—Processes yielding slags of special composition
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は転炉操業時に発生する2次ダストの有効な回収
法を目的とする転炉操業法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for operating a converter, which aims to effectively recover secondary dust generated during the operation of a converter.
従来の技術
従来該2次ダストの回収法として、高炉ダスト、転炉ダ
ストを主原料に、ロータリーキルン等で、重油またはガ
スを用いてペレット化する方法〔鉄と鋼Vou、7B
(1!37B)344B ) 、または燃料費低減を目
的とし、セメント等の固型材を使用したコールドペL/
ット化技術〔鉄と鋼VasL、76 (197B)S4
32〕により、得られたペレットを高炉または転炉で使
用するダスト回収方法が報告されている。Conventional technology Conventionally, as a method for recovering the secondary dust, a method of pelletizing blast furnace dust or converter dust as the main raw material using heavy oil or gas in a rotary kiln or the like [Tetsu-to-Hagane Vou, 7B]
(1!37B) 344B), or cold pellets using solid materials such as cement for the purpose of reducing fuel costs.
Cutting technology [Tetsu to Hagane VasL, 76 (197B) S4
[32] reported a dust recovery method in which the obtained pellets are used in a blast furnace or converter.
発明が解決しようとする問題点
転炉操業において、操業時に発生する排ガス中には約5
0〜80mmg/m”のダストが含まれており、ダスト
成分の約60%は鉄分であるため、転炉装入鉄合計の1
.4〜1.6%前後の鉄ロスが発生し、製出鋼歩留の悪
化要因となっており製造原価に与える影響も大きい。即
ち発生ダストを補集しダストの再利用を図る事は、鉄分
の回収で製出鋼歩留を向上させ製造原価の低減につなが
るものである。これらの事から発生ダストの鉄分を回収
する事は極めて重要な事である。Problems to be solved by the invention During converter operation, approximately 5
0 to 80 mmg/m'' dust is included, and approximately 60% of the dust component is iron, so 1 of the total iron charged in the converter is
.. Iron loss of around 4 to 1.6% occurs, which is a factor in deteriorating the steel production yield and has a large impact on manufacturing costs. In other words, collecting the generated dust and reusing the dust improves the yield of steel production by recovering the iron content, leading to a reduction in manufacturing costs. For these reasons, it is extremely important to recover the iron content of the generated dust.
しかるに補集されたダストは湿式除塵機で補集されるた
め、脱水処理を行った後でも約20〜30%の水分を保
有し、高熱溶銑中にそのまま投入使用する事は非常に危
険である。However, since the collected dust is collected by a wet dust remover, it retains about 20 to 30% moisture even after dehydration treatment, and it is extremely dangerous to use it by directly inserting it into high-temperature hot metal. .
そこで従来法では水分を除去する目的で天日乾燥を行い
、乾燥時にダスト中の成分FeOが酸化反応してFe2
O3に移行することを利用して、鉄鉱石の代替として炉
上より炉内に投入使用しているが、粉体であるため原料
ホッパー内での棚吊、投入時の原料歩留の低下、取扱い
時の粉塵の問題があった。Therefore, in the conventional method, drying is carried out in the sun for the purpose of removing moisture, and during drying, the component FeO in the dust undergoes an oxidation reaction and becomes Fe2.
Utilizing the transition to O3, it is used as a substitute for iron ore by charging it into the furnace from above the furnace, but since it is a powder, it is suspended in the raw material hopper, and the raw material yield decreases at the time of charging. There was a problem with dust during handling.
またこれらの問題を解決するため前記セメント等の固型
材を使用したり、焼結処理を行って、固型の状態で使用
する方法があるが、固型材の成分(S)等の影響で通常
操業時全チャージに使用し難く、また加工費等が高くな
る等の欠点があった。In order to solve these problems, there is a method of using a solid material such as cement, or sintering it and using it in a solid state, but due to the influence of the component (S) of the solid material, etc. It has drawbacks such as being difficult to use for all charges during operation and increasing processing costs.
問題点を解決するための手段
本発明はこれらの欠点を解消し、簡単に安価な方法でダ
ストを再利用し、溶鋼歩留の向上を図り、製造原価を低
減させる優れた方法を提供しようとするものであり、そ
の要旨とするところは、転炉操業時に発生する湿潤2次
ダスI・を、−上底吹転炉に前装入し、底吹き不活性ガ
スによる不活性雰囲気中で、前回吹錬後の炉体残熱によ
り、該湿潤2次ダストを脱水した後、溶銑を装入し吹錬
する事を特徴とする転炉吹錬法である。Means for Solving the Problems The present invention aims to eliminate these drawbacks and provide an excellent method for easily and inexpensively reusing dust, improving the yield of molten steel, and reducing manufacturing costs. The gist is that the wet secondary dust I generated during converter operation is pre-charged into a top-bottom blowing converter, and then heated in an inert atmosphere with a bottom-blowing inert gas. This is a converter blowing method characterized by dehydrating the wet secondary dust using the residual heat of the furnace body after the previous blowing, and then charging and blowing hot metal.
作用 本発明は次の特徴を有する。action The present invention has the following features.
(イ)上底吹転炉炉内を不活性ガス雰囲気状態に保ち、
炉内で湿潤2次ダストを前回吹錬後の炉体残熱により、
該湿潤2次ダストを脱水した後、溶銑を装入する、従来
法に比べて非常に簡単な方法である。(a) Maintaining the inside of the top-bottom blowing converter furnace in an inert gas atmosphere,
Due to the residual heat of the furnace body after the previous blowing of wet secondary dust in the furnace,
This method is much simpler than the conventional method, in which hot metal is charged after dewatering the wet secondary dust.
(ロ)使用ダスト内FeOの酸化を不活性ガスにて抑制
する事で冷却係数を低下させ、鉄鉱石の代替を行った場
合、従来法と比べて使用量が増えるので、溶鋼歩留の向
上効果が著しい利点が有る。(b) By suppressing the oxidation of FeO in the used dust with an inert gas, the cooling coefficient is lowered and when iron ore is replaced, the amount used increases compared to the conventional method, so the yield of molten steel is improved. It has the advantage of being highly effective.
(ハ)加工を加えないで使用できるため、原料コス)・
が低く、またダスト中の有効成分の再利用が効果的にで
き、不純物(S)等の影響も少ない利点が有る。(c) Raw material cost as it can be used without any processing)・
It also has the advantage of being low, the effective ingredients in the dust can be reused effectively, and the influence of impurities (S) etc. is small.
(ニ)使用ダスト内FeOを未酸化の状態で使用できる
ため、前装入が可能であり、溶銑装入時に異常反応が起
きない安全性の高い使用方法である。(d) Since the FeO in the dust used can be used in an unoxidized state, pre-charging is possible, and it is a highly safe usage method that does not cause abnormal reactions during charging of hot metal.
次に本発明方法の実施に使用する装置例を説明する。第
1図において、上底吹転炉l内に湿潤ダストを装入、底
吹ノズル2より不活性ガス3を吹込み、炉口蓋4にて炉
内を密閉し、前回吹錬後の炉体残熱により該湿潤2次ダ
ストを昇熱、ダスト水分を除去した後、溶銑を装入し操
業を行うものである。Next, an example of an apparatus used to carry out the method of the present invention will be explained. In Fig. 1, wet dust is charged into a top-bottom blowing converter l, an inert gas 3 is blown in from a bottom-blowing nozzle 2, the inside of the furnace is sealed with a furnace cover 4, and the furnace body after the previous blowing is After the wet secondary dust is heated by the residual heat and the dust moisture is removed, hot metal is charged and the operation is carried out.
次に本発明方法の実施例を挙げる。Next, examples of the method of the present invention will be given.
実施例1
170を転炉において、予め底吹ノズル保護ガス(N2
)を用い、炉内を不活性雰囲気に保ち、ダスト成分(w
t%) : T−Fe 54.19. FeO45,
8、Fe2O318,3、CaO9,1、S O,0
13、C2,3、Mn 1.8、水分5.5ノ湿潤2次
ダストを4.1を装入後、炉口蓋を使用して炉口を密閉
、炉内雰囲気温度650℃の状態で強制乾燥した。Example 1 In a converter, a bottom-blowing nozzle protective gas (N2
) to maintain an inert atmosphere inside the furnace and remove dust components (w
t%): T-Fe 54.19. FeO45,
8, Fe2O318,3, CaO9,1, SO,0
13, C2,3, Mn 1.8, moisture 5.5 After charging 4.1 with wet secondary dust, the furnace mouth was sealed using the furnace mouth cover, and the furnace atmosphere temperature was 650°C. Dry.
次いで、溶銑配合率86.7%、溶銑温度1357°C
1溶銑中のSi濃度27X10−2%の溶銑を装入、吹
錬を実施した結果、比較材(ダストを使用しない通常操
業材、N=15回行なったもの)に比べて溶鋼歩留1.
21%の増効果を得る事ができた。尚、本チャージの吹
止成分は問題なく、スラグ滓化状況についても良好であ
った。Next, the hot metal blending ratio was 86.7%, and the hot metal temperature was 1357°C.
1.As a result of charging and blowing hot metal with a Si concentration of 27X10-2%, the molten steel yield was 1.
We were able to obtain an increased effect of 21%. The blow-off component of this charge had no problems, and the slag formation was also good.
比較例1
170を転炉において、予め実施例1と同様に保護ガス
にて炉内を不活性雰囲気に保ち、
ダスト成分(wt%) : T−Fe 53.77、F
e00.4、Fe2O373,?、Can 10.3、
S O,05、CO,4、Mn 1.[l、水分1.
5の天日乾燥ダストを4.4を装入後、実施例1と同様
に炉内強制乾燥した。Comparative Example 1 170 was placed in a converter, and the inside of the furnace was kept in an inert atmosphere using protective gas in the same manner as in Example 1. Dust components (wt%): T-Fe 53.77, F
e00.4, Fe2O373,? , Can 10.3,
SO, 05, CO, 4, Mn 1. [l, moisture 1.
After charging the sun-dried dust No. 5 to No. 4.4, it was force-dried in the furnace in the same manner as in Example 1.
次いで、溶銑配合率87.5%、溶銑温度1341”0
、溶銑中のSi濃度22X10−2%の溶銑を装入した
ところ、装入面異常反応が起き、フレームが大量に発生
、非常に危険な状態となった。この事はFe2O3の分
解反応で、溶銑中の(C)と分解0が反応したものと思
われる。Next, the hot metal blending ratio was 87.5%, and the hot metal temperature was 1341”0.
When hot metal with a Si concentration of 22 x 10-2% was charged, an abnormal reaction occurred on the charging surface and a large amount of flames were generated, creating a very dangerous situation. This seems to be a decomposition reaction of Fe2O3, in which (C) in the hot metal reacted with decomposition 0.
また溶鋼歩留は比較材(ダストを使用しない通常操業材
、N=15回行ったもの)に比べて、1.23%の増効
果を得た。また吹止成分、スラグ性状とも問題はなかっ
た。In addition, the molten steel yield was increased by 1.23% compared to the comparison material (normally operated material without using dust, conducted N = 15 times). Furthermore, there were no problems with the blow-off component and slag properties.
しかしこの方法は途中でフレームが発生し、定常の作業
として難があり、又粉体供給もホッパー内づまり等がと
きおり発生し、定常の安定操業としては適当でなかった
。However, this method caused flames to occur during the process, making it difficult to operate on a regular basis, and clogging of the hopper occasionally occurred during the supply of powder, making it unsuitable for stable, regular operation.
比較例2
170を転炉においてセメント材を用いて固型化したペ
レット材を、炉上副原料ホッパーに装入し、ペレット化
ダスト成分(wt%) : T−Fe 49.8、F
ee O,4、Fe2O387,?、Ga015.8、
S O,+4 、 C0036、Mn L、S、水分
1.0のダストを炉」二より鉄鉱石の代替として使用。Comparative Example 2 Pellet material obtained by solidifying 170 using cement material in a converter was charged into the auxiliary raw material hopper on the furnace, and pelletized dust component (wt%): T-Fe 49.8, F
ee O,4, Fe2O387,? , Ga015.8,
S O,+4, C0036, Mn L, S, dust with a moisture content of 1.0 was used as a substitute for iron ore in the furnace.
次いで、溶銑配合率97.0%、溶銑温度1360°C
1溶銑中のSi濃度32X10−2%、S 30 Xl
0−2%の溶銑を装入し、吹錬を実施、ペレットダスト
を5.4t/ch炉上より1次投入、使用を行った結果
、溶鋼歩留は比較材(ダストを使用しない通常操業材、
N=15回行なったもの)に比べて1.08%の増効果
を得る事ができたが、吹止成分(S)値が60XIO−
2%と高くアフタープローをする結果になった。Next, the hot metal blending ratio was 97.0%, and the hot metal temperature was 1360°C.
1 Si concentration in hot metal 32X10-2%, S 30 Xl
As a result of charging 0-2% hot metal, performing blowing, and using pellet dust as the primary charge from the top of the 5.4 t/ch furnace, the molten steel yield was lower than that of the comparative material (normal operation without using dust). wood,
We were able to obtain an increase effect of 1.08% compared to the test (N = 15 times), but the blowout component (S) value was 60XIO-
The result was a high after-plow of 2%.
発明の効果
本発明の転炉吹錬法によれば従来方法に比較して簡単に
安価な方法でダストを再利用し、ダスト中有効成分の回
収で溶鋼歩留の向上、生石灰原単位の低減、LDG回収
増等の効果が得られ、製造原価に及ぼす効果はきわめて
大きい。Effects of the Invention According to the converter blowing method of the present invention, dust can be reused in a simpler and cheaper manner than conventional methods, and the active ingredients in the dust can be recovered to improve the yield of molten steel and reduce the unit consumption of quicklime. , increased LDG recovery, etc., and the effect on manufacturing costs is extremely large.
第1図は本発明方法を実施するために使用する装置例の
説明図である。
l・・・上底吹転炉、2・・・底吹ノズル、3・・・不
活性ガス、4拳・・炉口蓋、5・Φ・ダスト。FIG. 1 is an explanatory diagram of an example of an apparatus used to carry out the method of the present invention. l...Top and bottom blowing converter, 2...bottom blowing nozzle, 3...inert gas, 4 fists...furnace mouth cover, 5, Φ, dust.
Claims (1)
前装入し、底吹き不活性ガスによる不活性雰囲気中で、
前回吹錬後の炉体残熱により、該湿潤2次ダストを脱水
した後、溶銑を装入し吹錬する事を特徴とする転炉吹錬
法。The wet secondary dust generated during converter operation is pre-charged into a top-bottom blowing converter, and is then heated in an inert atmosphere created by bottom-blowing inert gas.
A converter blowing method characterized in that the wet secondary dust is dehydrated using the residual heat of the furnace body after the previous blowing, and then hot metal is charged and blowing is performed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP211785A JPS61163204A (en) | 1985-01-11 | 1985-01-11 | Converter blowing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP211785A JPS61163204A (en) | 1985-01-11 | 1985-01-11 | Converter blowing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61163204A true JPS61163204A (en) | 1986-07-23 |
JPH0564207B2 JPH0564207B2 (en) | 1993-09-14 |
Family
ID=11520404
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP211785A Granted JPS61163204A (en) | 1985-01-11 | 1985-01-11 | Converter blowing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61163204A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009079256A (en) * | 2007-09-26 | 2009-04-16 | Jfe Steel Kk | Method for utilizing recovered dust in waste gas from converter, in iron-making process |
KR20200044878A (en) * | 2017-11-22 | 2020-04-29 | 스미토모 긴조쿠 고잔 가부시키가이샤 | Method of disposing of lithium ion battery waste material |
-
1985
- 1985-01-11 JP JP211785A patent/JPS61163204A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009079256A (en) * | 2007-09-26 | 2009-04-16 | Jfe Steel Kk | Method for utilizing recovered dust in waste gas from converter, in iron-making process |
KR20200044878A (en) * | 2017-11-22 | 2020-04-29 | 스미토모 긴조쿠 고잔 가부시키가이샤 | Method of disposing of lithium ion battery waste material |
Also Published As
Publication number | Publication date |
---|---|
JPH0564207B2 (en) | 1993-09-14 |
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