JPS61213309A - Manufacture of flux for refining using molten pig iron dephosphorization slag as starting material - Google Patents
Manufacture of flux for refining using molten pig iron dephosphorization slag as starting materialInfo
- Publication number
- JPS61213309A JPS61213309A JP60053266A JP5326685A JPS61213309A JP S61213309 A JPS61213309 A JP S61213309A JP 60053266 A JP60053266 A JP 60053266A JP 5326685 A JP5326685 A JP 5326685A JP S61213309 A JPS61213309 A JP S61213309A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- flux
- refining
- hot metal
- pig iron
- 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
- C21C5/36—Processes yielding slags of special composition
-
- 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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
- C21C1/025—Agents used for dephosphorising or desulfurising
-
- 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
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/076—Use of slags or fluxes as treating agents
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は溶銑脱Pスラグを原料とする精錬用フラツクス
の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for producing a refining flux using dephosphorized hot metal slag as a raw material.
(従来の技術)
溶銑脱Pスラグは転炉スラグに較べP2O,が高いと言
う特徴を有するが、燐肥に含まれるP20!1はどでは
ないのでそのまま燐肥として使用することはできない。(Prior Art) Hot metal dephosphorized slag has a characteristic of having higher P2O than converter slag, but since the P20!1 contained in phosphorus fertilizer is not found in phosphorus fertilizer, it cannot be used as is as phosphorus fertilizer.
また、通常の転炉スラグは道路用材や土木用材に一部利
用されているが、脱Pスラグはc、o/SiO□が高く
崩壊性が強いため、このような用途にも使用できない。In addition, some ordinary converter slag is used for road materials and civil engineering materials, but dephosphorized slag has a high c, o/SiO□ content and is highly collapsible, so it cannot be used for such purposes.
一方、製鋼における品質ニーズから溶銑予備処理、転炉
吹錬、2次精錬および連続鋳造などの工程で使用する精
錬用フラックスは需要増加の方向にある。このような背
景のもと溶銑脱Pスラグを再生利用する試みが種々なさ
れてきた。例えば脱Pスラグを粉砕し、浮遊選鉱法によ
ってp、os濃度が高い部分と低い部分に分離して、P
2O,が高い部分を燐肥に、低い部分を高炉原料に有効
利用する方法(特開昭58−61210)、および脱P
スラグに炭素質または炭素を含む溶鉄を添加して、脱P
処理温度以上の温度で還元処理し、溶鉄中にPを移行さ
せた後のスラグを脱P用フラックスに再生利用する方法
、(特開昭59−53637)などが提案されている。On the other hand, demand for refining flux used in processes such as hot metal pretreatment, converter blowing, secondary refining, and continuous casting is on the rise due to quality needs in steelmaking. Against this background, various attempts have been made to recycle dephosphorized hot metal slag. For example, dephosphorization slag is crushed and separated into parts with high and low concentrations of p and os using the flotation method.
A method of effectively using the high 2O content for phosphorus fertilizer and the low 2O content for blast furnace raw material (Japanese Patent Application Laid-open No. 58-61210), and dephosphorization.
DeP by adding carbonaceous or carbon-containing molten iron to slag
A method has been proposed (Japanese Unexamined Patent Publication No. 59-53637) in which slag is recycled into flux for removing P after performing a reduction treatment at a temperature higher than the treatment temperature and transferring P into the molten iron.
(発明が解決しようとする問題点)
しかし、前者は浮遊選鉱するためスラグを微小に破砕す
る必要があり能率的でない。また、P濃度が低い部分に
しても精練補助剤に使用できるほど低くないので例えば
高炉原料など用途が限定される等の問題がある。一方、
後者はアルカリ土類金属の酸化物とハロゲン化物からな
る低融点の特殊な脱S7ラツクスを用いて処理した脱P
スラグを対象としたものであり、CaO系の溶銑脱Pス
ラグに社運用できない。また、これらはスラグを脱P再
生する方法であるが脱P後のスラグ組成および特性を積
極的にコントロールしようとするものではない。(Problems to be Solved by the Invention) However, the former method is inefficient because it is necessary to crush the slag into small pieces for flotation. In addition, even if the P concentration is low, it is not low enough to be used as a scouring aid, so there is a problem that its use, for example, as a blast furnace raw material, is limited. on the other hand,
The latter is a dephosphorization process using a special low-melting-point deS7 laxative made of alkaline earth metal oxides and halides.
It is intended for slag and cannot be used for CaO-based hot metal dephosphorization slag. Further, although these are methods for dephosphorizing and regenerating slag, they do not attempt to actively control the slag composition and characteristics after dephosphorization.
(問題点の解決手段)
本発明は、この溶銑脱Pスラグを溶融還元してPを除去
するとともに積極的に改質処理して、用途別に適正な組
成、特性をもった精錬用フラックスの製造を目的とする
ものであり、その要旨は次の通りである。(Means for Solving Problems) The present invention melts and reduces this hot metal dephosphorization slag to remove P and actively modifies it to produce a refining flux with an appropriate composition and characteristics for each use. Its purpose is as follows.
500℃以上の溶銑脱Pスラグに炭素質還元剤を添加す
るとともに、一方、5102、A1.O3、C,F、、
Mならびに、その化合物からなる改質剤の中から1種以
上を選択的に添加して溶融還元処理および改質処理を行
なうことを特徴とする精錬用フラックスの製造方法。While adding a carbonaceous reducing agent to hot metal dephosphorization slag at 500°C or higher, on the other hand, 5102, A1. O3, C, F...
1. A method for producing a refining flux, which comprises selectively adding one or more modifiers selected from M and a modifier made of its compound to perform melt reduction treatment and modification treatment.
(作用) 以下、本発明の詳細について説明する。(effect) The details of the present invention will be explained below.
製鋼工程で使用する精錬用フラックスは、例えば脱Sフ
ラックス、脱S7ラツクス、酸化防止剤など多種があり
、それぞれ用途別に適正な組成、特性が付与されている
。具体的な例をあげて説明すると湯面酸化防止、介在物
吸着等を目的とする取鍋フラックスおよび連鋳パウダー
基材は非酸化性でCaO/5i02が1.0前後の低融
′点組成が好まれ、脱SフラックスはCaO/Ag2O
3が1.0もしくは3.5前後で、同じく非酸化性の低
融点組成が望まれるなどである。また、溶銑予備処理の
発達とともに転炉のスラグ量が減少しており、従来の脱
P、脱S目的からヒユームの発生防止、スピッティング
防止などの役割りが重視され、リサイクルスラグもそれ
に適したものが求められている。There are many types of refining fluxes used in the steelmaking process, such as S-free fluxes, S7-free fluxes, and antioxidants, each of which has an appropriate composition and characteristics depending on its use. To give a specific example, the ladle flux and continuous casting powder base material for the purpose of preventing oxidation of the hot water surface, adsorbing inclusions, etc. are non-oxidizing and have a low melting point composition with CaO/5i02 around 1.0. is preferred, and the S removal flux is CaO/Ag2O
3 is around 1.0 or 3.5, and a non-oxidizing, low melting point composition is also desired. In addition, with the development of hot metal pretreatment, the amount of slag in converters is decreasing, and the role of prevention of fume generation and spitting is becoming more important than the conventional purpose of removing P and S, and recycled slag is also suitable for these purposes. something is wanted.
一方、スラグを再生利用するには先ずPを除去する必要
がある。スラグの脱Pは高温で炭素還元すると比較的容
易に行なわれるが、従来は溶鉄に移行するP分が多く、
高リン溶鉄の取扱いに問題があった。これに関し本発明
者は溶銑脱Pスラグから単独のPを分離、回収する方法
を別途開発した。この方法は、スラグの溶融還元におい
て溶鉄へ移行するP分を極力抑え、ガス状となる元素P
の発生比率を高め、これを回収することを特徴とするも
ので、溶銑脱PスラグのMnO含有量を5チから12%
の間になるように調節して、炭素質還元剤を添加すると
ともに5i02 、 Alto、ならびにその化合物か
らなるPの分離促進剤を選択的に添加して溶融還元処理
する方法であって、このPの分離促進剤が精錬用フラッ
クスの改質剤と共通している。したがってPの回収と併
せて、溶銑脱Pスラグを精錬用フラックスに改質処理す
ることは極めて経済的であり、好ましいと考えられる。On the other hand, in order to recycle slag, it is first necessary to remove P. Dephosphorization from slag is relatively easy through carbon reduction at high temperatures, but in the past, a large amount of P was transferred to molten iron;
There was a problem in handling high phosphorous molten iron. In this regard, the present inventor separately developed a method for separating and recovering individual P from hot metal dephosphorized slag. This method minimizes the amount of P that transfers to molten iron during slag reduction, and the element P that becomes gaseous.
This system is characterized by increasing the generation ratio of MnO and recovering it, increasing the MnO content of hot metal dephosphorized slag from 5% to 12%.
A method of melting and reducing the P by adding a carbonaceous reducing agent and selectively adding a P separation accelerator consisting of 5i02, Alto, and compounds thereof. The separation accelerator is the same as the modifier for refining flux. Therefore, in addition to recovering P, it is considered to be extremely economical and preferable to reform the dephosphorized hot metal slag into a refining flux.
本発明者はこのことに着目して、溶銑脱Pスラグを対象
に軟珪石、M灰ホタル石等の改質材を用いて幾多の脱P
、改質実験を行ない、次のような結果を得た。すなわち
、溶銑脱Pスラグに適正量の炭素質還元剤と5i02
、Al2O3、M−、CaF2 ならびにその化合物か
らなる改質剤の中から1種以上を選択的に添加して溶融
還元処理および改質処理すると、スラグ脱P率は改質剤
添加後のスラグ組成とよく整理できることが判明した。The present inventor has focused on this, and has carried out numerous dephosphorization processes using modifying materials such as soft silica stone and M fluorite.
We conducted a modification experiment and obtained the following results. That is, an appropriate amount of carbonaceous reducing agent and 5i02 are added to the hot metal dephosphorization slag.
, Al2O3, M-, CaF2, and their compounds. When one or more modifiers are selectively added to the melting reduction treatment and modification treatment, the slag dephosphorization rate is determined by the slag composition after the addition of the modifier. It turned out that it was possible to organize it well.
第1図によると精錬用フラックス、例えばCαo/51
o2が1.0前後の取鍋フラックスおよびCaO/Al
2O3が1.0前後の脱Sフラックスはスラグ脱Pの面
からも適正な組成であり、極めて好都合であることが知
られる。また、例えばCa O/Si 02 =3.0
前後の滓化促進剤ならびにCtz O//A1203
” 3.5前後の脱87ラツクスを製造するについても
前者には多少のAltOsk、後者は多少の8102を
添加して脱P率を向上することができる。According to Figure 1, the refining flux, e.g. Cαo/51
Ladle flux and CaO/Al with o2 around 1.0
It is known that a S-removal flux with 2O3 of around 1.0 has an appropriate composition from the viewpoint of slag removal and is extremely convenient. Also, for example, Ca O/Si 02 =3.0
Front and rear sludge accelerators and Ctz O//A1203
” When producing dephosphorized 87 lux of around 3.5, it is possible to improve the dephosphorization rate by adding some AltOsk to the former and some 8102 to the latter.
本発明は、この実験結果にもとすくものであり、溶銑脱
Pスラグを還元処理してPf除去するとともに、積極的
な成分調整によるスラグ改質を行ない精錬用フラックス
を製造する方法である。改質のだめの成分調整は溶銑脱
Pスラグを添加する改質剤の組成から計算できるし、同
様に融点調整についてもCcO−A1203系、CaO
−5i02 CaF2系などの多元系状態図から予測
して、実用的に所望の組成、特性を付加することができ
る。The present invention is based on this experimental result, and is a method for manufacturing flux for refining by reducing Pf from hot metal dephosphorization slag and reforming the slag by actively adjusting the components. The composition adjustment of the reforming tank can be calculated from the composition of the modifier to which the hot metal dephosphorization slag is added, and similarly, the melting point adjustment can be done using CcO-A1203 series, CaO
-5i02 Practically desired compositions and properties can be added by predicting from a multicomponent system phase diagram such as CaF2 system.
しかして、このようにして得られた精錬用フラックスに
還元処理のため非酸化性でかつ、溶融しているので品質
が均質である。本発明の実施および使用によって次のよ
うな利点が得られる。The refining flux obtained in this manner is non-oxidizing due to the reduction treatment, and is molten, so the quality is homogeneous. The implementation and use of the present invention provides the following advantages.
(1)従来、処置に困っていた溶銑腕Pスラグを完全有
効利用できる。(1) Hot metal arm P slag, which has traditionally been difficult to dispose of, can be used completely effectively.
(2)精錬用フラックスが所内供給できコスト低減がは
かれる。(2) Refining flux can be supplied within the plant, reducing costs.
(3)取鍋フラックスの使用により、合金歩留り、特に
M歩留りが向上する。(3) The use of ladle flux improves alloy yield, especially M yield.
(4)転炉リサイクルにより、吹錬初期の滓化が促進さ
れ、ひいては転炉スラグの崩壊性が改善される。(4) Converter recycling promotes slag formation at the initial stage of blowing, and thus improves the collapsibility of converter slag.
次に、溶銑腕Pスラグを溶銑還元処理および改質処理す
るためには大量のエネルギーを必要とするので処理コス
トが問題になるが、本発明はこれを解消するため原料の
溶銑腕Pスラグを500℃以上または溶融状態で溶融還
元炉に装入することを特徴とする。熱計算を行ないエネ
ルギー配分をみると原料スラグの昇熱、溶解が約45%
、改質剤の昇熱、溶解が約23チ、FelMn、Pなど
の還元熱が約23%を占めていることが判ったので、脱
Pスラグの顕熱利用を狙い脱Pスラグ温度測定を行なっ
た。スラグ6Tを鉄製容器に排出した場合のスラグ中心
部温度は排出直後で1100〜1200℃、5時間経過
後で1020〜1150℃、10時間経過後で1000
〜1100℃を示し温度低下が小さいことが確認できた
。スラグ排出量、輸送時間などの操業変動を勘案しても
脱Pスラグを500℃以上で溶融還元炉に装入すること
は十分可能である。一方装入温度が500℃以下では顕
熱利用効果が小さい。また、条件によっては溶融状態で
脱Pスラグを排出する場合もあるが、溶融状態で装入す
れば顕熱利用効果が一層大きいことは当然である。脱P
スラグを500℃以上または溶融状態で装入することに
より、溶融還元および改質処理に必要な熱エネルギーは
15〜43%低減でき、経済的効果が大きい。Next, processing cost becomes a problem because a large amount of energy is required to reduce and reform hot metal arm P slag, but in order to solve this problem, the present invention uses hot metal arm P slag as a raw material. It is characterized in that it is charged into a melting reduction furnace at a temperature of 500°C or higher or in a molten state. When we performed a thermal calculation and looked at the energy distribution, the heating and melting of the raw material slag accounted for approximately 45%.
It was found that the heat rise and melting of the modifier accounted for approximately 23%, and the reduction heat of FelMn, P, etc. accounted for approximately 23%, so we measured the dephosphorization slag temperature with the aim of utilizing the sensible heat of the dephosphorization slag. I did it. When slag 6T is discharged into an iron container, the temperature at the center of the slag is 1100-1200℃ immediately after discharge, 1020-1150℃ after 5 hours, and 1000℃ after 10 hours.
~1100°C, confirming that the temperature drop was small. Even if operational fluctuations such as slag discharge amount and transportation time are taken into account, it is fully possible to charge dephosphorized slag into a smelting reduction furnace at a temperature of 500° C. or higher. On the other hand, when the charging temperature is below 500°C, the sensible heat utilization effect is small. Also, depending on the conditions, the dephosphorized slag may be discharged in a molten state, but it is natural that the sensible heat utilization effect will be greater if it is charged in a molten state. De-P
By charging the slag at 500° C. or higher or in a molten state, the thermal energy required for melting reduction and reforming treatment can be reduced by 15 to 43%, which has a large economic effect.
(実施例) 次に、本発明の実施例について説明する。(Example) Next, examples of the present invention will be described.
容量500 KVAの電気炉を用いて、第1表に示す組
成の溶銑腕Pスラグを第2表に示す配合で溶融還元し脱
P、改質処理した。成品スラグの組成、脱P率および軟
化点を第3表に示す。第2表は配合目標および用途を併
示する。Using an electric furnace with a capacity of 500 KVA, hot metal arm P slag having the composition shown in Table 1 was melted and reduced according to the composition shown in Table 2 to remove P and undergo reforming treatment. Table 3 shows the composition, dephosphorization rate, and softening point of the finished slag. Table 2 also shows formulation goals and applications.
第1表
原料の配合調整により、はぼ配合狙い通りのC,O/
5102およびCaO/Al2O3を有し、かつ軟化点
の影響をうけるが、いずれも大きく除去されておシ例え
ば湯面酸化防止剤、脱SNJなどの精錬用フラックスお
よびその基材として使用できるものである。By adjusting the blend of raw materials in Table 1, the C, O/
5102 and CaO/Al2O3, and is affected by the softening point, but all of them are largely removed and can be used as a refining flux and its base material, such as as a hot water surface oxidation inhibitor and for removing SNJ. .
(発明の効果)
以上、詳述した如く、本発明は溶銑脱Pスラグを還元処
理してPを除去するとともに、改質処理を行ない精錬用
フラックス′を安価に製造する実質的な方法を提供する
ものである。なお、還元処理および改質処理において、
ガス攪拌を併用すると効果的である。(Effects of the Invention) As described in detail above, the present invention provides a practical method for reducing P-removal of hot metal dephosphorization slag and performing reforming treatment to produce refining flux' at low cost. It is something to do. In addition, in the reduction treatment and reformation treatment,
It is effective to use gas stirring together.
第1図は溶銑脱Pスラグの溶融還元における成グラフで
ある。
炙あ又噸陵整−FIG. 1 is a graph showing the formation of hot metal dephosphorized slag in melting reduction. Roasted Amata Giryo Preparation
Claims (1)
るとともに、一方SiO_2、Al_2O_3、CaF
_2、Alならびにその化合物からなる改質剤の中から
1種以上を選択的に添加して、溶融還元処理および改質
処理を行なうことを特徴とする精錬用フラックスの製造
方法。A carbonaceous reducing agent is added to hot metal dephosphorization slag at 500°C or higher, while SiO_2, Al_2O_3, CaF
_2. A method for producing a refining flux, characterized in that one or more modifiers selected from among modifiers consisting of Al and its compounds are selectively added to perform melting reduction treatment and modification treatment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60053266A JPS61213309A (en) | 1985-03-19 | 1985-03-19 | Manufacture of flux for refining using molten pig iron dephosphorization slag as starting material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60053266A JPS61213309A (en) | 1985-03-19 | 1985-03-19 | Manufacture of flux for refining using molten pig iron dephosphorization slag as starting material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61213309A true JPS61213309A (en) | 1986-09-22 |
JPH0524962B2 JPH0524962B2 (en) | 1993-04-09 |
Family
ID=12937957
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60053266A Granted JPS61213309A (en) | 1985-03-19 | 1985-03-19 | Manufacture of flux for refining using molten pig iron dephosphorization slag as starting material |
Country Status (1)
Country | Link |
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JP (1) | JPS61213309A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994019496A1 (en) * | 1993-02-23 | 1994-09-01 | Laporte Group Australia Limited | Insulating/metallurgical composite and method of manufacturing same |
KR20010060907A (en) * | 1999-12-28 | 2001-07-07 | 이구택 | BOP Slag dephosphorization |
KR100593685B1 (en) * | 1999-12-28 | 2006-07-03 | 주식회사 포스코 | Seleclive Reduclion Method of BOF Slages |
JP2012219298A (en) * | 2011-04-06 | 2012-11-12 | Jfe Steel Corp | Method for recovering iron and phosphorus from steelmaking slag |
CN102876839A (en) * | 2011-07-15 | 2013-01-16 | 武汉钢铁(集团)公司 | Low-silicon-aluminum-killed-steel-casting-slag-based refining agent and preparation method thereof |
-
1985
- 1985-03-19 JP JP60053266A patent/JPS61213309A/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994019496A1 (en) * | 1993-02-23 | 1994-09-01 | Laporte Group Australia Limited | Insulating/metallurgical composite and method of manufacturing same |
KR20010060907A (en) * | 1999-12-28 | 2001-07-07 | 이구택 | BOP Slag dephosphorization |
KR100593685B1 (en) * | 1999-12-28 | 2006-07-03 | 주식회사 포스코 | Seleclive Reduclion Method of BOF Slages |
JP2012219298A (en) * | 2011-04-06 | 2012-11-12 | Jfe Steel Corp | Method for recovering iron and phosphorus from steelmaking slag |
CN102876839A (en) * | 2011-07-15 | 2013-01-16 | 武汉钢铁(集团)公司 | Low-silicon-aluminum-killed-steel-casting-slag-based refining agent and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0524962B2 (en) | 1993-04-09 |
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