JPS5953613A - Method and device for treating steel making slag - Google Patents

Method and device for treating steel making slag

Info

Publication number
JPS5953613A
JPS5953613A JP16563282A JP16563282A JPS5953613A JP S5953613 A JPS5953613 A JP S5953613A JP 16563282 A JP16563282 A JP 16563282A JP 16563282 A JP16563282 A JP 16563282A JP S5953613 A JPS5953613 A JP S5953613A
Authority
JP
Japan
Prior art keywords
slag
steel making
mixture
steel
viscosity
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
Application number
JP16563282A
Other languages
Japanese (ja)
Other versions
JPS625220B2 (en
Inventor
Masao Tomari
泊 正雄
Minoru Matsuda
松田 稔
Hidetaka Oshima
大島 英孝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Jiryoku Senko Co Ltd
Original Assignee
Nippon Jiryoku Senko Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Jiryoku Senko Co Ltd filed Critical Nippon Jiryoku Senko Co Ltd
Priority to JP16563282A priority Critical patent/JPS5953613A/en
Publication of JPS5953613A publication Critical patent/JPS5953613A/en
Publication of JPS625220B2 publication Critical patent/JPS625220B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/36Processes yielding slags of special composition

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Furnace Details (AREA)

Abstract

PURPOSE:To fractionate the steel making slag in a molten state to a ground metal to be used as raw material for steel making and others by admixing a flux to said steel making slag to induce melting reaction and to decrease viscosity then dropping the slag onto a receiving tray made of steel and cooling quickly the slag and further subjecting the cooled slag to grinding, magnetic separation and sieving. CONSTITUTION:A receiving tray 1 consisting of a steel plate 3 projected with a frame body 2 for preventing overflow at the peripheral edge, is laid with refractory bricks 4 embedded in the places to receive the dropping molten mixture and is flowed with cooling water between the flat plates 2 and 3 is prepared. On the other hand, >=1 kind of silicate rock, ores, blast furnace slag, etc. are admixed at 5-30wt% to the steel making slag in a molten state contained in a vessel 10 for contg. the mixture to decrease the viscosity of the steel making slag by the melting reaction. The steel making slag having the decreased viscosity is dropped into the bricks 4 of said tray 1 and is quickly cooled to progress vitrification. The vitrified steel making slag is subjected to grinding, magnetic separation and sieving. Whereby the slag is fractionated to the ground metal to be used as raw material for steel making and the rest to be utilized for sand such as for sand blasting.

Description

【発明の詳細な説明】 本発明1.1 ?’l fN滓からの溶出水を中性に近
くかつ有害物質を含まない抑にし、またV、分等の有効
地金とそれ以外の物とに分別し該tlll金は製鋼原料
とし、それ以外の物はサンドブラスト用サンドや砂等へ
の有効利用を図ろうとする製轄滓の処理方法並びにその
装置に関するものである。
[Detailed Description of the Invention] Present invention 1.1? 'l The leached water from the fN slag is kept close to neutral and does not contain harmful substances, and is separated into effective metals such as V and slag and other materials, and the tllll gold is used as a raw material for steelmaking, and the other materials are This article relates to a method and apparatus for processing slag, which is intended to be effectively used as sand for sandblasting, sand, etc.

転炉滓はr及びβ−2CaOsSiO,、FeCsO(
3tfrNT石灰)主体でゲーレナイト(2CRO・A
、、/、03・S逼Ot)アケルマナイト(2CaO−
MgO−2SiO2) 、マグネタイト(Fe、04)
へマタイト(Fe、03 ) 、ウスタイ1 (Fe+
O)等を含有しでいる。特殊な転炉滓はペリクlノ・−
ス(MgO)を含有する場合もあり、オー1りl/−ブ
処理(ASTM法、2 FI 0℃、20に2/era
、3時u(I ffd持テ25−I 0−rq (7)
 PT1度で10M1:J下を崩壊物とする)を行なう
と約30JTjμ。
The converter slag is r and β-2CaOsSiO, FeCsO (
3tfrNT lime) and Gehlenite (2CRO/A
,,/,03・S〼Ot) Akermanite (2CaO-
MgO-2SiO2), magnetite (Fe, 04)
Hematite (Fe, 03), Ustai 1 (Fe+
O) etc. Special converter slag is produced by Pericles.
(MgO) may also be present, and the oven treatment (ASTM method, 2 FI 0°C, 20 to 2/era
, 3 o'clock u (I ffd holding te 25-I 0-rq (7)
If 1 degree PT and 10M1: J are used as decaying material, the result will be approximately 30 JTjμ.

%崩壊する、溶出試験を行なうとpIIは約110〜1
15を示す。
% disintegration, pII is about 110-1 when dissolution test is performed.
15 is shown.

11rl気炉滓は酸化押滓と還元押滓に大別され、前者
ハ/? 及ヒ(! 2C*O・S+O,ニ、10 ’l
i’ 1.t r −2CaO−8i02に富む場合と
3Cno・2 S t O!に富む場合があり、前者の
崩壊率は約10重量%以下、後者は冷却の過程で膨張崩
壊(ダスティング)シ、はと第7ど100重所%崩壊す
る、溶出試験を行なうとP■■は約11.0〜114を
示す。
11rl air furnace slag is roughly divided into oxidized slag and reduced slag, and the former is ha/? andhi (! 2C*O・S+O, ni, 10 'l
i' 1. t r −2CaO-8i02-rich case and 3Cno・2 S t O! The disintegration rate of the former is approximately 10% by weight or less, while the latter undergoes expansion disintegration (dusting) during the cooling process and disintegrates 100% by weight. ■ indicates approximately 11.0 to 114.

フェロクロム滓はスピネル(MgO・Sin、)フォル
ステライト(2Mg0@S 第02 )が主体でフール
シナイト(FeO@A403 ) エンスタタイト(M
ho@Sin、 )等を含有1し崩壊性はないが、Cr
、O,を約611員%〜7重犀え含有し%環境庁告示方
法で溶出するとクロムイオン総址で約0.lppm〜2
ppm溶出する。
Ferrochrome slag is mainly composed of spinel (MgO・Sin) forsterite (2Mg0@S No. 02), furcynite (FeO@A403), and enstatite (M
ho@Sin, ) etc.1 and has no disintegrability, but Cr
, O, containing about 611% to 7-membered chromium ions, and when eluted according to the method notified by the Environment Agency, the total amount of chromium ions is about 0.0%. lppm~2
Elutes ppm.

又、特殊ザ(1滓Lt r及びβ−2C:no−8:O
,、P’−CnO−2CaO−Mg0−2CaO−、2
CnOaAI、0s−8in、 +  テ(オフサイト
(CnO−R4gOψ2S sat )等全含有し、C
r、03ヲ約6重船X〜773. KL%含有し、同上
の方法で溶出゛するとクロムイオン紛片で約旧ppm−
・75p pm溶出し、かつ約781Hit%崩壊する
、溶出試験を行なうとpTIは約11.0〜115を示
す。
In addition, special za (1 slag Ltr and β-2C: no-8: O
,,P'-CnO-2CaO-Mg0-2CaO-,2
CnOaAI, 0s-8in, + Te (off-site (CnO-R4gOψ2S sat ), etc.), C
r, 03wo approx. 6 heavy ships X~773. Contains KL%, and when eluted using the same method as above, the chromium ion powder contains about 100 ppm-
- It elutes at 75 ppm and disintegrates at about 781 Hit%. When an elution test is performed, the pTI is about 11.0 to 115.

コ11う(7)崩? ノJi5t 因ハ、F−CnO、
MgO、’1CnO−8iO,、3CRO@2SiO2
によるものである。
Ko11u (7) collapse?ノJi5t Inha, F-CnO,
MgO,'1CnO-8iO,,3CRO@2SiO2
This is due to

本発明は上述の諸問題を解消し、溶融ay 6n re
が持つ顕熱を有効に利用し、−あるいはIJQ !!i
sのみで不舟する場合には必要に応じて夕1部熱を補J
r! I、 t″ツ9缶滓処理する方法及び装V(をl
ll1供1(A、と嘴ろものであり、その要旨は溶H1
1に態にあるシリf1りrり′に、珪酸塩質の岩石や鉱
物、赤泥、Jノラミ、1ツノ物廃砂、高炉スラグ、石炭
灰、ダストの一種以」二を5〜30市M%添加混合して
溶融反応を!1胆さけ粘性(IC下を生ぜ゛しめた後、
上記611合物が落下する部所に耐火れA、がを敷設し
内部に冷却水を召19通Trf能とした鉄ri+る。い
は毎製の受皿−ヒに放流せしめて急冷させガラス化を進
行さ・時、次いで破砕、at選、篩分けを行ない地金と
その他の物とに分別することを特徴とするjlllll
l1供1方法乃び溶融、状態にある製鋼汁と、珪酸塩質
の岩石や鉱物、赤泥、カラミ、鋳物高砂、高炉スラグ、
石廚灰、ダストの一睡以上との混合物収容容器と、同収
容容器を所襲(fr置まで揮びかつ収容混合物を上記受
皿」二に投入する運搬兼投入装置?’fと、上記混合物
が投入落下さ第1る部所には耐火れんがが敷設さ第1し
かも内部には冷却水導通路が形成された鉄あるいは鉗l
製の受皿と、同受用l」二で冷却凝固した混合物を回収
し次の破砕、磁選、篩分は工程へ搬送゛する搬送装置と
から構成される製餅・1坪の処理装置である。
The present invention solves the above-mentioned problems and improves melting ay 6n re
Effectively utilize the sensible heat of - or IJQ! ! i
If you have to abandon the ship with only s, supplement the evening heat as necessary.
r! I, Method and equipment for treating 9 can slag
ll1ku1 (A, and the beak, the gist of which is molten H1
Add 5 to 30 types of silicate rocks and minerals, red mud, J. slag, horn waste sand, blast furnace slag, coal ash, and dust to the soil in condition 1. Add M% and mix to initiate a melting reaction! 1 After creating the viscosity (IC),
A fire-resistant girder was laid at the place where the above 611 compound would fall, and cooling water was poured inside. It is characterized by discharging the metal into a saucer for each production to rapidly cool it and proceed with vitrification, followed by crushing, AT sorting, and sieving to separate the bullion and other materials.
Steelmaking juice in the 11 process or melting state, silicate rocks and minerals, red mud, karami, casting Takasago, blast furnace slag,
A container for containing a mixture of stone ash and dust, a transporting and charging device for carrying the container to a raiding place and dumping the contained mixture into the above-mentioned saucer; Refractory bricks are laid in the first place where the input falls, and inside the first place there is an iron or iron lug with a cooling water passage formed.
This is a 1 tsubo rice cake processing device that is comprised of a rice cake receiving tray and a conveying device that collects the cooled and solidified mixture in the same receiving tray and transports it to the next process for crushing, magnetic separation, and sieving.

上記した珪酸塩質の岩石や鉱物、赤泥、カラミ、鋳物高
砂、高炉スラグ、石炭灰、ダスト等の添加物を製鋼溶滓
中に添加する方法は下記の方法がある。
The following methods are available for adding additives such as the above-mentioned silicate rocks and minerals, red mud, karami, foundry sand, blast furnace slag, coal ash, and dust to steelmaking slag.

(i)  製作1炉内に製鋼の最初又は途中から投□入
する。
(i) Production 1 Inject steel into the furnace from the beginning or during the process.

■ Pi−炉に出1後投入する。■ Take it out to the Pi-furnace and then put it in.

■ 製鋼炉から排出する溶n沖、に接して投入する。■Put it in contact with the molten metal discharged from the steelmaking furnace.

■ ツM中炉から打出する溶滓汁の落下((f岡と接し
て投入する。
■ Falling of the molten slag from the medium furnace ((f) is thrown in contact with the oka.

(5)  排滓鏝の敷r¥の代用としで使用する。(5) Use it as a substitute for the slag removal trowel.

(a)iJj滓鋪内で溶滓と、サンドイッヂ状になる様
に投入する。
(a) Add the molten slag to the iJj slag in a sandwich-like manner.

■ (孕)■■■の方法で投入し、ランス状物を装入し
、バブリングガスを吹き込A、でバブリングを行なう。
■ (Pregnant) Charge according to the method of ■■■, insert a lance-shaped object, blow bubbling gas and perform bubbling with A.

(i)連鋳終了前の取鍋内に49゛入後、のろ鍋に排滓
する。
(i) After pouring 49゜ into the ladle before the end of continuous casting, drain the slag into a ladle.

なお、中性又は弱アルカリ性のスラグとずろためには」
−記添加物の添加負1が多いので、相熱を有効利用する
ため■(、S)<Vの方法が有効である。
In addition, for neutral or slightly alkaline slag and slag.
- Since there are many negative 1 additions of additives mentioned above, the method (2) (, S) < V is effective in order to effectively utilize the phase heat.

ここで、スラグが溶融状IJヒにJする間S io、 
、 A/40゜及びFe2O3等を含有する上述の未利
用冑源や産業廃棄物を添加するのは、溶融シ17 fi
滓の断熱を有効に利用するためであり、添加物と17で
S r 02あるいはA/、、0.のみでも充分である
が、8i0. 、 A、/!、(1,単味では溶融温度
が高いので反応が生起し叶い欠点がある。
Here, while the slag is in the molten state,
, A/40° and the above-mentioned unused armament sources and industrial waste containing Fe2O3 etc. are added to the melting system 17 fi.
This is to effectively utilize the heat insulation of the slag, and with the additive and 17 S r 02 or A/, 0. Although it is sufficient to use only 8i0. , A, /! , (1) Since the melting temperature is high when used alone, reactions occur and there is a drawback.

次に本発明のy、Im滓の処11方法についての実験結
果について以下に記載する。
Next, experimental results regarding the 11 methods for treating y and Im slag of the present invention will be described below.

まず第1表は、本実験に使用する原料つ化学分析値(重
ル・%)を示1ノたものである。
First, Table 1 shows the chemical analysis values (weight/%) of the raw materials used in this experiment.

これらの試料を105〜110℃の恒温乾燥機で24時
間以上乾燥後、製侑滓と赤泥等添加物質は→ノンプルグ
ラインダーで3訓以」二に狛]砕後(但し、ダストは微
細なためその才まの粒度で)、製鎖性についてのみ磁選
して、更に03部以下に組枠してゼーゲル錐を作り、溶
但濡度を1f111定した。その結果を第2表に示す。
After drying these samples in a constant temperature dryer at 105-110℃ for more than 24 hours, the additives such as slag and red mud were crushed with a non-pull grinder for 3 or more times (however, fine dust was removed). Therefore, with the grain size of the grain), magnetic selection was carried out only for chain-forming properties, and the siegel cone was made by framing to 03 parts or less, and the weld wetness was determined to be 1f111. The results are shown in Table 2.

又、同試料を使用して、ルツボ回転式粘度測定機で絶対
粘度を各温度毎にt111定した。その結果を第6表に
示す。
Further, using the same sample, the absolute viscosity was determined at t111 at each temperature using a crucible rotation type viscosity measuring device. The results are shown in Table 6.

なJゴ、3−以下の磁選尾鉱等を電、融マグネSノアル
ツボに入れて、  1550℃に1′1持しj:シリコ
ニット田、気炉で15分間保持して溶解後、赤泥、珪酸
塩質の岩石等の添加物を投入し7、約3分移にルツボを
+1V、り出して第1図、第2図に丙、す如^受冊(1
)上にその厚さが約20削となるべく拡’fL! /i
Q汗、し、急冷さ→1、該急冷rト固物をその粒径が5
−以下となるべく破砕して、その比重、溶出試験、ビッ
カース硬ハ(等を測定した。その結果を第4表及び第5
表に示す。なお比較の為に1卓料滓についての性状を第
6表に、又原料rンの溶出試駒結114を第7表にそi
lぞイl示ず。
Put the magnetic tailings, etc. of 3- or less into an electric, fused magnetite crucible and hold it at 1550℃ for 15 minutes. Add additives such as silicate rocks, etc. 7. After about 3 minutes, take out the crucible at +1V, and as shown in Figures 1 and 2,
) on top so that its thickness is about 20 millimeters wide 'fL! /i
Q sweat, rapid cooling → 1, the rapid cooling solid material has a particle size of 5
- The specific gravity, elution test, Vickers hardness, etc. were measured by crushing the pieces as much as possible.The results are shown in Tables 4 and 5.
Shown in the table. For comparison, the properties of 1-table material slag are shown in Table 6, and the elution test sample 114 of raw material R is shown in Table 7.
I don't know what to do.

1(J−i、前記第4表に示す各試ネlの全てについて
F・Cooの含有fitはo、on 1+r鉛え、又そ
の簡明率は000m j、lXでJ)った。
1 (J-i, the content of F.Coo was o, on 1+r for all of the test samples shown in Table 4 above, and the simplification rate was 000mj, lxJ).

又第4表及び第6表に記載した生成含有鉱物の略称は下
記の曲りである。
The abbreviations of the minerals listed in Tables 4 and 6 are as follows.

sp・・・・・・・・・MgO拳A/、20゜FO・・
・・・・・・・2Mg0−8iO。
sp......MgO fist A/, 20°FO...
......2Mg0-8iO.

En・・・・・・・・・MgO・Si02Mf・・・・
・・・・・MgO・F/!、0゜β−C,S・・・β−
2CaO・S i02γ−C,S ・−r−2C,0a
sis。
En......MgO・Si02Mf...
...MgO・F/! ,0゜β-C,S...β-
2CaO・S i02γ-C,S・-r-2C,0a
sis.

AK・・・・・・・・・2C内0−MgO−28iO。AK......0-MgO-28iO in 2C.

Ge  −−−−2CaO−A40.−8iO。Ge---2CaO-A40. -8iO.

C^S・・・・・Cll5 FIICRO=−Free++Ca0 Jlu・・・・・・・・・Fe、0.。C^S...Cll5 FIICRO=-Free++Ca0 Jlu...Fe, 0. .

Mg・・・・・・・・・F’ e 30゜Wu  ・・
・・・・・・・FfIO C,A−= −” ・’ 3C1OIIA4(13又上
記第5表に示した生成物につき、Cu+T@Cr + 
Cd 、 Ph 、 Zn 、 FH、!4n 、 A
s 、 Tangについても溶出イオン濃度を測定した
が、それら全でについて検出されなかった。又上記第7
表に示した原料については、T−Cr及びFuイオンの
他にCu 、 Crl 、 Pb 、 Zn 、 R4
n 、 AII、 T*I]、gにつき溶出イオン潤度
を測定したが全てについてそれらのイオンは検出されな
かった。
Mg・・・・・・F' e 30゜Wu...
......FfIO C,A-=-"・'3C1OIIA4 (13Also, for the products shown in Table 5 above, Cu+T@Cr+
Cd, Ph, Zn, FH,! 4n, A
The eluted ion concentrations of s and Tang were also measured, but none of them were detected. Also, the above 7th
Regarding the raw materials shown in the table, in addition to T-Cr and Fu ions, Cu, Crl, Pb, Zn, R4
n, AII, T*I], and g, but these ions were not detected in all of them.

次に本発明装置について図面を参酌しながら説明すわば
、溶融製鋼滓と赤泥等添加物の溶融混合物を急冷する為
の受皿(1)は、第1図及び第2図に示す様に、周縁部
に溢出防Jll用枠体(2)がある晶さをもって突設さ
11た鉄J)るいは鋼製の平板(3)であって、溶融混
合物を注下する部所には面1人れんが(4)をJ!+!
設状に敷設している。そしてt!あるいは鋼製の平板は
2枚の平板がある間隔をもって平行に対設されておりそ
第1ら各平板間にIi例えば■バQllllの如き間隔
住持用リブ(5)が各所に複数段配設され(キ)す、そ
の様にして形成さ−また2枚の平11ii間の空間部(
6)に冷却水を流通せしめ得る様になっている。図示の
物にあっては受皿の終端部側に給水用パイプf71をそ
の両端ITrl C1部が受皿(1)の両側に出る如く
通し、該給水用パイプ(7)の両イク14から給水し、
tl″f1パイプ側壁に成膜した多数の穴から空間部(
6)へ給水し受皿(1)の混合物注下側に同様にその両
藺開「1部が受皿(1)の両側に出かっその側れYには
多数の穴がV)設された排水用パイプ(8)内へ流、シ
込みその両端から排水する如き構造のものである。なお
受皿(1)の周縁部の枠体(2)の中でりll111の
終端部(第1し1で右端部)に位置するものは、第2図
に示す様にその基端部を回転軸(9)により回動自をに
軸YlさJlるものとしておき、混合物が冷却凝固した
後にジオペルあるいはスフレパー等ii1’i ’M、
j ″F段で該冷却混、合物をIIV出す114合に便
なら17める14:+ tr +/ζ、おく。
Next, the apparatus of the present invention will be explained with reference to the drawings.The receiving tray (1) for rapidly cooling the molten mixture of additives such as molten steel slag and red mud is as shown in FIGS. A flat plate (3) made of iron or steel with a sharp protruding frame body (2) for preventing overflow on the periphery, and a surface 1 is provided at the part where the molten mixture is poured. J the brick (4)! +!
It is laid in the shape of a building. And t! Alternatively, two flat plates made of steel are arranged in parallel with each other at a certain interval, and between the first and each flat plate, a plurality of ribs (5) for maintaining the distance are arranged at various places. The space between the two flat plates (11ii) is formed in this way.
6) allows cooling water to flow through it. In the illustrated example, a water supply pipe f71 is passed through the terminal end side of the saucer so that both ends of the water supply pipe F71 are exposed on both sides of the saucer (1), and water is supplied from both holes 14 of the water supply pipe (7).
tl″f1 The space (
6) Water is supplied to the lower side of the saucer (1) where the mixture is poured, and a portion of the mixture is poured onto both sides of the saucer (1). The structure is such that the water flows into the pipe (8), sinks in, and drains from both ends of the drain pipe (8). As shown in Fig. 2, the base end of the one located at the right end (right end) should be able to rotate around the rotating shaft (9), and after the mixture has cooled and solidified, the Souffleper etc.ii1'i'M,
If the cooling mixture is discharged to IIV in stage F, 14: + tr +/ζ is set for 17 hours.

次に本発明ν・閾の全枠を第3図に示ず、即ち況合物収
容賽器01は】m常溶滓輪t)るいは取ハ等称される耐
熱v1容器であり、それを送行台車若しくはり1ノーン
等から成る運搬11(投入装置01)で運搬しかつ−1
,述の受1111 (11面上に溶融沖、合物を注下す
るものである。また受m1(1)の終端部より伜か蘭れ
かつややThには耐熱性コンベヤ若しくはその他の搬送
装(Bayrが配置せしめられており受1711 fl
>、 J:で冷却凝固した混合物をジオペル若しくはス
フ1ツバー等所要手段で該iIR送装鍔0り上に載架し
次工程へ移す如き構成とされている。ここで次工程とは
破砕、磁選、篩分は工程のことであり、それらは公知の
方法をIf4 聾回数繰返し行なう。
Next, the entire framework of the present invention ν/threshold is not shown in FIG. -1 is transported by transport 11 (loading device 01) consisting of a transport cart or beam 1-noon, etc.
, above mentioned receiver 1111 (This is for pouring the molten mixture onto surface 11. Also, from the end of receiver m1 (1), a heat-resistant conveyor or other conveyance device is installed from the end to the end. (Bayr is placed and Uke 1711 fl
>, J: The mixture cooled and solidified is placed on the iIR feeding collar using a necessary means such as a diopel or sufu tube and transferred to the next step. Here, the next steps are crushing, magnetic separation, and sieving, and these steps are performed by repeating known methods several times.

次に具体的な実施例を示す。Next, specific examples will be shown.

この実施例は、ニル一式11v気炉に転炉滓、特殊薊1
滓等を500に9入れて溶解し、山間時の溶融スラグ沖
に接して5那ρ)下の粘板岩fe 5Qk7、又は出湯
前の炉内に粘板岩; fI7物陥砂7o9i : 3[
]%配合物を投入後、取鍋Iζ受けてクレーンIl吊っ
て、第1図に示す急冷装置に放流した。
This example is a complete set of 11v air furnace, converter slag, special
Melt slag etc. in 500 and melt it, slate fe 5Qk7 below in contact with the molten slag in the mountains, or slate in the furnace before tapping;
] After adding the mixture, the ladle Iζ was lifted by a crane Il, and the mixture was discharged into the quenching apparatus shown in FIG.

約20〜30分後に放流、スラグI、1手テ、′さオ)
ねる渇IWとなり、放流性の層厚は放油、位置イ・1町
で約35rtn、他の部分は20〜0.5 cmとなっ
た。
After about 20 to 30 minutes, discharge, slag I, 1 hand, 'Sao)
The thickness of the discharge layer was approximately 35 rtn at the I-1 town, and 20 to 0.5 cm in other areas.

このスラグをジョークラッシャーで破砕後(約15F以
十)磁選し、尾鉱は更にロールクラッシャー(間隔的5
−)で粉砕し、篩イ)け後、サンドブラストのサンド試
験、アスコン用2111骨材試験、細砕物は路盤材試験
、オーlりlフープによる崩#試験(ASTM法で10
〜25門につき処理(7,10胛以下を粉化物とした)
又、環境庁告示方法による溶出試験等を行ない、第8表
に示す。
After crushing this slag with a jaw crusher (approximately 15F or more), the tailings are further crushed with a roll crusher (at intervals of 5
-) and sieved, sandblasting sand test, 2111 aggregate test for ascon, crushed material test for roadbed material, and crushing test using an all-hole hoop (ASTM method: 2111 aggregate test)
~25 seeds were treated (less than 7.10 seeds were treated as powder)
In addition, elution tests were conducted according to the method notified by the Environment Agency, and the results are shown in Table 8.

トノ」−述べて来た様に本発明によれば、シリ炉滓に珪
酸j14質岩石をはじめとする1:、述の添加物を適量
/6\加している為にその融点がPliシく低干し従っ
て粘性が低下し反応が十分に行なえること、及びその後
の水冷受皿を用いた装置rtによる角冷で混合物はその
大半がガラス化される為にlI’d jjGj性1.t
なく、有害イオンの溶出1才防11されか−〕P11も
中性に近いイ1自となる。
As described above, according to the present invention, an appropriate amount of the additives mentioned above, including silicic acid J14 rock, is added to the silicate furnace slag, so that the melting point of the silicate furnace slag reaches Pli silicon. The viscosity is lowered and the reaction can be carried out sufficiently, and most of the mixture is vitrified by the subsequent cooling using an apparatus rt using a water-cooled saucer. t
There is no elution of harmful ions, and P11 is also close to neutral.

従って地金を除いたその他のものも→Jシンドブラスト
サンド(適度の鋭角を持ち研掃力が大)、土蛙月1の砂
、路盤材、ケーソンの中込め材等あらゆる分野に利)t
l t、 19るものである。
Therefore, other materials other than bare metal are also useful in all fields, such as J-sindo blast sand (moderately sharp angle and great abrasive power), Tsuchigazuki 1 sand, roadbed material, caisson filling material, etc.)
lt, 19.

更に又受皿内を流通する冷却水が′−jえら第1ろ熱−
rオルギーは適宜の熱交1!J!器4・用いイ1効に利
用しく;Iるものである。
Furthermore, the cooling water flowing in the saucer is
r Orgy is appropriate heat exchange 1! J! 4. Use: 1. It is useful for effective use.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は不発間装PIの受皿の一部Lll欠平面図、第
2図は第1図A−A絆に於ける1411面図、第3図は
本発明装置Nの全体概萼図。 図中、(1):受皿 01:混合物収容容器 (Ill :運搬兼投入装置西 Oダニ搬送装y7 特許出願人  日本磁力選鉱株式会社
FIG. 1 is a partly cutaway plan view of the saucer of the unexploded intercalator PI, FIG. 2 is a 1411-view view taken along the line A-A in FIG. 1, and FIG. 3 is a general schematic view of the device N of the present invention. In the figure, (1): Receiving tray 01: Mixture storage container (Ill: Transporting and charging device West O mite transporting device y7 Patent applicant: Japan Magnetic Mineral Sensing Co., Ltd.

Claims (1)

【特許請求の範囲】 1、 溶融状態にある製鋼滓に、畦酸塩質の岩石や鉱物
、赤泥、カラミ、鋳物高砂、^炉スラグ、石炭灰、ダス
トの一種以上を5〜30重絨%添加混合して溶融反応を
生起させ粘性低下を生ぜしめた後、上記混合物が落下す
る部所に耐火れんがを敷設し内部に冷却水を流通可能と
した鉄あるいは#+!製の受皿上に放流せしめて急冷さ
せガラス化を進行させ、次いで破砕、磁選、篩分I3を
行ない地金とその他の物とに分別することを特数とする
!ll!l創滓の処理方法。 2 溶融状態にある!P!!州滓と、月;酸塩質の岩石
や鉱物、赤泥、カラミ、鋳物高砂、高炉スラグ、石炭灰
、ダストの一種以上との混合物収容容器と、同収界容器
を所要位置まで運びかつ収容混合物を下記受皿上に投゛
入する運搬31(扮入装植と、」二記混合物が投入落下
される部所には耐火れんがが敷設されしかも内部には冷
却水導通路が形成された鉄あるいは鉛製の受皿と、同受
皿]二で冷却凝固した混合物を回収し次の破砕、磁選、
篩分は工程へ搬送する搬送装置とから構成されるIJI
I裔11滓の処理袋−0
[Scope of Claims] 1. 5 to 30 heavy carpets of one or more of the following are added to the molten steel slag: porphyry rocks and minerals, red mud, karami, cast iron sand, furnace slag, coal ash, and dust. % added and mixed to cause a melting reaction and a decrease in viscosity, and then firebricks were laid in the area where the above mixture would fall, allowing cooling water to flow inside the iron or #+! The special feature is to discharge the water onto a stainless steel tray and rapidly cool it to proceed with vitrification, followed by crushing, magnetic separation, and sieving I3 to separate the metal from other materials! ll! l How to dispose of sludge. 2 It is in a molten state! P! ! A container containing a mixture of slag and one or more of the following: acid rocks and minerals, red mud, karami, cast iron sand, blast furnace slag, coal ash, and dust, and the ablution container are transported to the required location and stored. Transport 31 (loading and loading) of throwing the mixture onto the tray described below (2. Alternatively, a lead saucer and the same saucer] collect the cooled and solidified mixture for the next crushing, magnetic separation,
IJI consists of a transport device that transports the sieve to the process.
I Descendant 11 Slag Processing Bag-0
JP16563282A 1982-09-22 1982-09-22 Method and device for treating steel making slag Granted JPS5953613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16563282A JPS5953613A (en) 1982-09-22 1982-09-22 Method and device for treating steel making slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16563282A JPS5953613A (en) 1982-09-22 1982-09-22 Method and device for treating steel making slag

Publications (2)

Publication Number Publication Date
JPS5953613A true JPS5953613A (en) 1984-03-28
JPS625220B2 JPS625220B2 (en) 1987-02-03

Family

ID=15816047

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16563282A Granted JPS5953613A (en) 1982-09-22 1982-09-22 Method and device for treating steel making slag

Country Status (1)

Country Link
JP (1) JPS5953613A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6184011A (en) * 1984-09-29 1986-04-28 Osaka Denki Kk Coil spool for transformer and the like
JPS6183876A (en) * 1984-09-29 1986-04-28 日本磁力選鉱株式会社 Method of treating steel-making dephosphorized slag
US6848973B2 (en) 2003-03-06 2005-02-01 Sable Des Forgens Method for blast cleaning using ilmenite tailing particles
US7132093B2 (en) 2002-06-05 2006-11-07 UNIVERSITé LAVAL Mesoporous mixed oxide materials as a new class of SO2 resistant catalysts for hydrocarbon oxidation
CN109553313A (en) * 2018-12-10 2019-04-02 攀枝花钢城集团有限公司 Steel slag recoverying and utilizing method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108686828B (en) * 2018-05-29 2021-03-19 湖南埃铝环保科技有限公司 Method for separating, extracting iron and removing sodium from red mud

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6184011A (en) * 1984-09-29 1986-04-28 Osaka Denki Kk Coil spool for transformer and the like
JPS6183876A (en) * 1984-09-29 1986-04-28 日本磁力選鉱株式会社 Method of treating steel-making dephosphorized slag
US7132093B2 (en) 2002-06-05 2006-11-07 UNIVERSITé LAVAL Mesoporous mixed oxide materials as a new class of SO2 resistant catalysts for hydrocarbon oxidation
US6848973B2 (en) 2003-03-06 2005-02-01 Sable Des Forgens Method for blast cleaning using ilmenite tailing particles
CN109553313A (en) * 2018-12-10 2019-04-02 攀枝花钢城集团有限公司 Steel slag recoverying and utilizing method

Also Published As

Publication number Publication date
JPS625220B2 (en) 1987-02-03

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