JPS59123706A - Treatment of desulfurized slag - Google Patents
Treatment of desulfurized slagInfo
- Publication number
- JPS59123706A JPS59123706A JP57231028A JP23102882A JPS59123706A JP S59123706 A JPS59123706 A JP S59123706A JP 57231028 A JP57231028 A JP 57231028A JP 23102882 A JP23102882 A JP 23102882A JP S59123706 A JPS59123706 A JP S59123706A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- raw material
- sieve
- crushed
- desulfurization
- 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
- 239000002893 slag Substances 0.000 title claims abstract description 59
- 239000002994 raw material Substances 0.000 claims abstract description 21
- 238000005245 sintering Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 9
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 9
- 239000004571 lime Substances 0.000 claims abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 claims description 28
- 230000023556 desulfurization Effects 0.000 claims description 28
- 239000002184 metal Substances 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 13
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 7
- 238000001816 cooling Methods 0.000 abstract description 6
- 239000006148 magnetic separator Substances 0.000 abstract description 5
- 229910000831 Steel Inorganic materials 0.000 abstract description 4
- 239000010959 steel Substances 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 3
- 229910052742 iron Inorganic materials 0.000 abstract description 3
- 239000010953 base metal Substances 0.000 abstract description 2
- 239000007921 spray Substances 0.000 abstract 2
- 101150006573 PAN1 gene Proteins 0.000 abstract 1
- 230000003009 desulfurizing effect Effects 0.000 abstract 1
- 238000012216 screening Methods 0.000 abstract 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 6
- 238000007885 magnetic separation Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000007873 sieving Methods 0.000 description 3
- 239000004480 active ingredient Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 229940043430 calcium compound Drugs 0.000 description 1
- 150000001674 calcium compounds Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B3/00—General features in the manufacture of pig-iron
- C21B3/04—Recovery of by-products, e.g. slag
- C21B3/06—Treatment of liquid slag
- C21B3/08—Cooling slag
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/022—Methods of cooling or quenching molten slag
- C21B2400/024—Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/032—Separating slag from liquid, e.g. from water, after quenching
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/066—Receptacle features where the slag is treated
- C21B2400/07—Receptacle features where the slag is treated open to atmosphere
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/066—Receptacle features where the slag is treated
- C21B2400/072—Tanks to collect the slag, e.g. water tank
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Furnace Details (AREA)
Abstract
Description
【発明の詳細な説明】
(技術分野)
この発明は、溶銑の脱硫工程において発生する脱硫スラ
グの有効利用を図るための処理方法に関し、より詳しく
は、溶銑を転炉で軟線して鋼を製造する直前の工程にて
1、溶銑中にカルシウム化合物たとえば焼石灰を添加し
、溶銑脱硫を実施した時に発生する石灰系の脱硫スラグ
を有効利用可能にするもので、スラグ中の地金分を有効
に回収すると共に、残滓を高炉原料ないし焼結原料とし
て利用する処理方法を提供しようとするものである。Detailed Description of the Invention (Technical Field) The present invention relates to a treatment method for effectively utilizing desulfurization slag generated in the desulfurization process of hot metal, and more specifically, to a method for manufacturing steel by softening hot metal in a converter. In the step immediately before the hot metal desulfurization, 1. Calcium compounds such as burnt lime are added to the hot metal, making it possible to effectively utilize the lime-based desulfurization slag generated when hot metal desulfurization is carried out. The aim is to provide a processing method for recovering the residue and utilizing the residue as a blast furnace raw material or sintering raw material.
(従来技術)
高炉スラグ、転炉スラグの処理、有効利用については各
方面で多大の努力が払われ、近年これらの活用の目途が
立っている現状にあるが、脱硫スラグの処理、有効利用
については、未だ根本的な解決法が提示されていない。(Prior art) A great deal of effort has been made in various fields for the treatment and effective use of blast furnace slag and converter slag, and in recent years there are prospects for their use.However, regarding the treatment and effective use of desulfurization slag No fundamental solution has been proposed yet.
わずかに特開昭55−119137号公報にはソーダ灰
を用いた脱硫工程において生成するソーダ灰脱硫スラグ
から地金を回収する技術が提示されるにとどまる。JP-A-55-119137 only discloses a technique for recovering metal from soda ash desulfurization slag produced in a desulfurization process using soda ash.
この原因は石灰系脱硫スラグにつき、次の詫点にある。The cause of this lies in the following points about lime-based desulfurization slag.
(1)石灰系脱硫スラグの粒度分布、化学成分は表1.
2に示すように、大塊、微粉を含み、そのハンドリング
処理が困難なこと及び硫黄の含有量が高いことから、T
Fe 、 CaOなどの有効成分の回収が困難なこと。(1) Particle size distribution and chemical composition of lime-based desulfurization slag are shown in Table 1.
As shown in Figure 2, T
Difficulty in recovering active ingredients such as Fe and CaO.
表1 脱硫スラグの粒度分布、化学成分表2
(2)そのため破砕、篩分けを繰り返し、鉄分の一部を
磁選により回収し、大半の残滓は廃棄せざるを得ないこ
と。Table 1 Particle size distribution and chemical composition of desulfurization slag 2 (2) Therefore, crushing and sieving are repeated, a portion of the iron content is recovered by magnetic separation, and most of the residue must be discarded.
(発明の目的)
この発明は上記のようGこ大量廃棄が余儀なくされり脱
硫スラグについて有利な処理により、有効利用を目指し
た開発成果を開示するものである。(Object of the Invention) The present invention discloses the development results aimed at the effective use of desulfurization slag, which has been forced to be disposed of in large quantities as described above, through advantageous treatment.
(発明の構成)
この発明は、溶銑の脱硫工程で生じた石灰系脱硫スラグ
を溶滓鍋に排出し、次いで水分飽和状態に至るまで注水
冷却し、しかる後屋外に払い出して乾燥させた後、その
乾燥滓をふるい分けし、ふるい目10〜25mmのふる
い上につき、磁選して地金分を回収したのち、破砕処理
して、高炉原料または上記ふるい下とともに焼結原料に
供することGこより、前記課題を有利に解決するもので
ある。(Structure of the Invention) This invention discharges lime-based desulfurization slag produced in the desulfurization process of hot metal into a slag pot, then cools it by pouring water until it reaches a moisture saturated state, and then discharges it outside to dry. The dried slag is sieved, placed on a sieve with a sieve mesh size of 10 to 25 mm, subjected to magnetic separation to recover the metal content, and then crushed and used as a sintering raw material together with the blast furnace raw material or the bottom of the sieve. It solves problems advantageously.
この発明は、上記方法において溶滓鍋に排出された溶融
スラグに対し、とくに水分飽和状態に至るまで注水を行
って冷却を図り、この冷却過程をとることによって乾燥
後の脱硫スラグの磁選が極めて容易になることの発見に
由来している。This invention aims to cool the molten slag discharged into the slag ladle in the above method by injecting water until it reaches a moisture saturated state, and by using this cooling process, magnetic separation of the desulfurized slag after drying is extremely effective. It originates from the discovery that things can become easier.
すなわち、上述注水冷却を採ることによって鍋から屋外
に払い出される脱硫スラグは、水分含有量の多い凝固塊
、粉となり、しかも地金は粗粒部に集中して含有される
凝固形態をとる。That is, the desulfurization slag that is discharged outdoors from the pot by using the above-mentioned water injection cooling becomes a coagulated lump or powder with a high water content, and the base metal is concentrated in the coarse particles.
従って粗粒部分を選択して磁選すれば、効率良く地金の
回収が行われることになり、しかも細粒部分は地金混入
が極めて少ないことでも処理上有利である。Therefore, if the coarse grain portion is selected and subjected to magnetic separation, the ingots can be recovered efficiently, and the fine grain portion is advantageous in terms of processing because it contains very little ingots.
この発明では、上記冷却ののち、屋外にて多湿スラグの
乾・燥を図り、水分5〜20%程度まで適度に乾燥した
脱硫スラグを、次工稈のふるい分は工程に送給する。In this invention, after the above-mentioned cooling, the humid slag is dried outdoors, and the desulfurized slag that has been appropriately dried to a moisture content of about 5 to 20% is sent to the next culm sieve to the process.
このふるい工程で5%以上の水分値であれば、粉の飛散
なく、また20%以内の含湿ではふるいの目詰りも生ぜ
ず、ふるい分は処Jljが容易である。If the moisture content is 5% or more in this sieving step, there will be no scattering of powder, and if the moisture content is less than 20%, the sieve will not be clogged, and the sieve material can be easily disposed of.
またこのふるい分は工程においては、前述したように′
@を粒部Gこ地金分が多いことに注目して乾燥後にl脱
硫スラグを]0〜2Qmrn稈曳に分級し、ふるい下x
)11粒粉(ゴそのまま、焼結設備の原料として供給す
る。In addition, this sieve is used in the process as described above.
Noting that the grain part G has a high metal content, after drying, the desulfurization slag is classified into 0 to 2Q mrn culm and sieved.
) 11-grain powder (supplied as is as raw material for sintering equipment.
この焼結設備は排煙脱硫設備を具備するものを用いて大
気中へSOXの放散することなく有効成分を回収すると
共に、焼結生産性の向上および品質の改善を図れる。This sintering equipment is equipped with flue gas desulfurization equipment, so that active ingredients can be recovered without dispersing SOX into the atmosphere, and sintering productivity and quality can be improved.
一方地金分の多い粗粒分け、磁選および破砕処理し、地
金分を回収し、その残滓は、元の細粒分と併わせ焼結用
原料もしくは高炉用原料に利用され得る。On the other hand, the raw metal content is separated by coarse granulation, magnetic separation, and crushing treatment to recover the raw metal content, and the residue can be used as a raw material for sintering or a raw material for blast furnaces, together with the original fine grain content.
(具体例) この発明に従う脱硫滓の処理フローを第1図Gこ示す。(Concrete example) The processing flow of desulfurization slag according to the present invention is shown in FIG. 1G.
溶銑鍋から溶滓鍋1に分離排出をした石灰系溶融スラグ
2は溶滓鍋1内で水分飽和状態まで完全に注水して冷却
する(第1図(a))。水分飽和状態とは要は水びたし
にすることであり、溶滓鍋に水をあふれるまで注水する
。The lime-based molten slag 2 separated and discharged from the hot metal ladle into the slag ladle 1 is cooled by completely injecting water into the slag ladle 1 until it is saturated with water (FIG. 1(a)). Moisture saturation means water-soaking, which means pouring water into the slag pot until it overflows.
冷却後屋外ヤードに排出した含湿スラグ2′は、以後の
処理が容易な様に、例えば天日で約1ケ月間放置し水分
5〜20%まで乾燥させる(第1図(′b))。After cooling, the moist slag 2' discharged to the outdoor yard is left for about a month in the sun to dry to a moisture content of 5 to 20% so that subsequent treatment is easy (Fig. 1 ('b)). .
次に水分5〜20%程度に乾燥した脱硫スラグを、ふる
い目10〜2Qimの振動ふるい3でふるい上分2′と
ふるい子分2″とに分級する(第1図(C))。Next, the desulfurized slag dried to a moisture content of about 5 to 20% is classified into an upper sieve portion 2' and a lower sieve portion 2'' using a vibrating sieve 3 having a mesh size of 10 to 2 Qim (FIG. 1(C)).
上記の範囲の水分に調整されたスラグは廃棄やふるいの
目詰りなどのトラブルは発生しない。Slag whose moisture content is adjusted to the above range does not cause problems such as disposal or clogging of sieves.
上記のふるい分けにより約5〜40%がふるい上分2′
として残留し、このオーバーサイズについては、磁選機
4.により地金分5を回収しく第1図(d))、この例
で残滓6は破砕機7(第1図(e))を介して整粒し、
高炉原料もしくけ第1図(C)におけるふるい下分2N
アンダーサイズと混合して焼結原料に供する。Approximately 5 to 40% of the above sieving results in the top 2'
For this oversize, magnetic separator 4. In this example, the residue 6 is sized through a crusher 7 (Fig. 1(e)),
Lower sieve portion 2N in blast furnace raw material sieve Figure 1 (C)
It is mixed with undersize and used as a sintering raw material.
一方60〜95%発生するふるい下分2″を直接焼結用
原料8に供するのであり、ここにふるい目を焼結原料の
最大粒径とすることで、破砕工稈は不用になる。On the other hand, the sieve bottom fraction 2'', which is generated at 60 to 95%, is directly provided to the sintering raw material 8, and by making the sieve mesh the maximum particle size of the sintering raw material, a crushing culm is unnecessary.
脱硫スラグ中の地金と残滓の分離方法Gこついては、振
動ふるい3でオーバーサイズとしてふるい分はうした脱
硫スラグを、細裂の回転ドラム9に通し、このドラム通
過中にスラグ中の地金分選回収するため、回転ドラム9
中で残滓を破砕することがのぞましく、回転ドラム9が
らでた破砕スラグを磁選機4にがけ、地金分5として回
収し、残滓6は、もとのふるいに帰すようにしてもよい
(第1図(d’) >。このように回転ドラム9を磁選
機4との間に配設し、ふるい上分2′のオーバーサイズ
につき、磁選留分を増やすこともできる。Separation method of metal and residue in desulfurization slag G In case of trouble, the desulfurization slag that has been sieved as oversize with the vibrating sieve 3 is passed through a rotating drum 9 with fine cracks. Rotating drum 9 for sorting and collection
It is desirable to crush the residue inside the rotary drum 9, and the crushed slag from the rotating drum 9 can be passed through the magnetic separator 4 to be recovered as the bullion 5, and the residue 6 can be returned to the original sieve. (Fig. 1(d')) In this way, by disposing the rotating drum 9 between the magnetic separator 4 and the oversize of the upper sieve portion 2', it is also possible to increase the magnetic separator fraction.
第2図に脱硫スラグを使用した焼結鋼試験結果の一例を
示す。Figure 2 shows an example of the results of a sintered steel test using desulfurization slag.
この焼結原料に供される脱硫スラグは、表3に化学成分
を示す製鋼用溶銑の予備処理によって生成したもので、
スラグの化学成分は表4に示し、コークス添加%を併記
した。The desulfurization slag used as the sintering raw material is produced by preliminary treatment of hot metal for steelmaking, the chemical composition of which is shown in Table 3.
The chemical composition of the slag is shown in Table 4, and the percentage of coke addition is also listed.
表8
表4
このスラグは溶滓鍋に受けて直ちに注水冷却し、屋外に
て1ケ月間野積みで放置したとき水分7%となった。こ
の乾燥スラグをふるい目15闘の振動ふるいで分級し、
ふるい下分はそのまま、ふるい上分は磁選により鉄分を
回収(120”9/)ン)し、クラッシャで破砕し、ふ
るい下分に混合し7た。Table 8 Table 4 This slag was immediately cooled by pouring water into a slag pot, and when it was left to pile up outdoors for one month, the moisture content became 7%. This dried slag is classified using a vibrating sieve with 15 mesh sizes,
The lower part of the sieve was left as is, and the upper part of the sieve was subjected to magnetic separation to recover iron (120"9/min), crushed with a crusher, and mixed with the lower part of the sieve.
これらの混合物は、OL式焼結機に使用される通常の焼
結原料に対して、表4中0.8印については7.5%、
△印については5.0%を占めるように配合して焼結鍋
試験を行った。These mixtures are 7.5% for the 0.8 mark in Table 4, with respect to the normal sintering raw materials used in the OL type sintering machine.
For those marked with △, the sintering pot test was conducted with the mixture so as to account for 5.0%.
第2図○、Φ印に示すように脱硫スラグ混入率の増加は
、JPU指数で表示した点火前の通気抵抗の微小または
僅少な低下のもとに、焼結時間が低減し、また還元粉化
率RDI−3のわずかな低下において、落下強度(シャ
ッタ値)、生産高および歩留りの向上が実現される。As shown in Figure 2 ○ and Φ, an increase in the desulfurization slag mixing rate is due to a slight or slight decrease in the ventilation resistance before ignition expressed by the JPU index, a reduction in sintering time, and a reduction in reduced powder Improvements in drop strength (shutter value), production and yield are realized with a slight reduction in the conversion ratio RDI-3.
このように発明の方法により脱硫スラグ中のCaOを活
用し、通常の焼結原料や高炉原料としての石灰石の節約
に役立ち、また同じ<Fe分は鉄鉱石の節約Gこ寄与し
て、焼結鉱の生産能率の向上、にも大幅に貢献すること
ができる。In this way, the method of the invention makes use of CaO in the desulfurization slag, helping to save limestone as a normal sintering raw material and blast furnace raw material. It can also significantly contribute to improving ore production efficiency.
以上のようにしてこの発明によれば、石灰系脱硫スラグ
の処理の有効利用を有利に実現できる。As described above, according to the present invention, the treatment of lime-based desulfurization slag can be effectively utilized.
第1図はこの発明の実施態様を示す処理フロー図、 第2図は焼結鋼試験結果を示す線図である。 特許出願人 川崎製鉄株式会社 FIG. 1 is a processing flow diagram showing an embodiment of the present invention; FIG. 2 is a diagram showing the results of a sintered steel test. Patent applicant: Kawasaki Steel Corporation
Claims (1)
Gこ排出し、次いで水分飽和状態に至るまで注水冷却し
、しかる後屋外に払い出して乾燥させた後、その乾燥滓
をふるい分けし、ふるい目10〜25關のふるい上につ
き、磁選および破砕処理して、高炉原料または上記ふる
い下とともに焼結原料に供することを特徴とする脱硫ス
ラグの処理方法。1. Discharge the lime-based desulfurization slag produced in the desulfurization process of hot metal into the slag ladle G, then cool it by pouring water until it reaches a moisture saturated state, then take it outside to dry, and then sieve the dried slag, A method for treating desulfurization slag, which comprises magnetically separating and crushing the upper part of a sieve having 10 to 25 mesh sizes, and providing it as a blast furnace raw material or a sintering raw material together with the lower part of the sieve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57231028A JPS59123706A (en) | 1982-12-28 | 1982-12-28 | Treatment of desulfurized slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57231028A JPS59123706A (en) | 1982-12-28 | 1982-12-28 | Treatment of desulfurized slag |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS59123706A true JPS59123706A (en) | 1984-07-17 |
Family
ID=16917129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57231028A Pending JPS59123706A (en) | 1982-12-28 | 1982-12-28 | Treatment of desulfurized slag |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59123706A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100423440B1 (en) * | 1999-12-28 | 2004-03-19 | 주식회사 포스코 | Method for separating metal from steel-making slag |
| JP2008095167A (en) * | 2006-10-16 | 2008-04-24 | Nippon Steel Corp | Powder granulation method using desulfurized slag |
| JP2012072473A (en) * | 2010-09-29 | 2012-04-12 | Jfe Steel Corp | Raw material for blast furnace, and method for manufacturing the same |
| JP2018141196A (en) * | 2017-02-27 | 2018-09-13 | Jfeスチール株式会社 | Method for sorting steel slag, method for reusing steel slag, and method for producing raw materials for iron making |
| CN113083492A (en) * | 2021-03-30 | 2021-07-09 | 黄石市旺新环保科技有限公司 | Steelmaking solid waste integrated treatment system |
-
1982
- 1982-12-28 JP JP57231028A patent/JPS59123706A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100423440B1 (en) * | 1999-12-28 | 2004-03-19 | 주식회사 포스코 | Method for separating metal from steel-making slag |
| JP2008095167A (en) * | 2006-10-16 | 2008-04-24 | Nippon Steel Corp | Powder granulation method using desulfurized slag |
| JP2012072473A (en) * | 2010-09-29 | 2012-04-12 | Jfe Steel Corp | Raw material for blast furnace, and method for manufacturing the same |
| JP2018141196A (en) * | 2017-02-27 | 2018-09-13 | Jfeスチール株式会社 | Method for sorting steel slag, method for reusing steel slag, and method for producing raw materials for iron making |
| CN113083492A (en) * | 2021-03-30 | 2021-07-09 | 黄石市旺新环保科技有限公司 | Steelmaking solid waste integrated treatment system |
| CN113083492B (en) * | 2021-03-30 | 2022-09-13 | 黄石市旺新环保科技有限公司 | Steelmaking solid waste integrated treatment system |
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