JPS591227B2 - Method and device for producing spherical expanded slag - Google Patents

Method and device for producing spherical expanded slag

Info

Publication number
JPS591227B2
JPS591227B2 JP55047229A JP4722980A JPS591227B2 JP S591227 B2 JPS591227 B2 JP S591227B2 JP 55047229 A JP55047229 A JP 55047229A JP 4722980 A JP4722980 A JP 4722980A JP S591227 B2 JPS591227 B2 JP S591227B2
Authority
JP
Japan
Prior art keywords
slag
gutter
water
blast furnace
curved
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.)
Expired
Application number
JP55047229A
Other languages
Japanese (ja)
Other versions
JPS56142806A (en
Inventor
郁夫 魚住
猛 古賀
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.)
Hamada Heavy Industries Co Ltd
Original Assignee
Hamada Heavy Industries 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 Hamada Heavy Industries Co Ltd filed Critical Hamada Heavy Industries Co Ltd
Priority to JP55047229A priority Critical patent/JPS591227B2/en
Publication of JPS56142806A publication Critical patent/JPS56142806A/en
Publication of JPS591227B2 publication Critical patent/JPS591227B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • C21B3/08Cooling slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/026Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/062Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/066Receptacle features where the slag is treated
    • C21B2400/072Tanks 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)
  • Glanulating (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Manufacture Of Iron (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 本発明は、高炉滓を原料として軽くて表面気孔の少い球
形スラグの製造方法及び装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing light spherical slag with few surface pores using blast furnace slag as a raw material.

従来、高炉溶滓は冷却に際し溶滓中の硫化物が酸化され
、膨張する性質を有していることがら、この性質を利用
して膨張スラグを作る研究は、各所で多くの人によって
なされてきたが、界面に気孔を多く残さないこと、球形
にするという点は解決されず、現在に至っているのが実
情である。
Conventionally, blast furnace slag has the property of expanding when the sulfides in the slag are oxidized when cooled, and many people in various places have conducted research to utilize this property to create expanded slag. However, the problem of not leaving many pores at the interface and making it spherical has not been solved, and the reality is that this has remained the case to this day.

元来、高炉溶滓は、前述したように冷却に際し溶滓中に
含まれているSが大気中の02にあって酸化膨張するも
のであることから、表面気孔の少い球形の膨張スラグを
得る方法は冷却や飛散技術の問題に帰するものである。
Originally, blast furnace slag was made into spherical expanded slag with few surface pores because the S contained in the slag oxidized and expanded in the atmosphere during cooling as described above. The method of obtaining it comes down to problems with cooling and dispersion techniques.

本発明は、かかる観点から従来技術を見直した結果、そ
の主たる原因(表面気孔の少い球形の膨張スラグが得ら
れない)は、スラグの温度、粘度のコントロール、スラ
グ流量、流形のコントロール及び水量のコントロール並
びに遠方にとばすための飛散方式に問題のあることを知
った。
As a result of reviewing the prior art from this perspective, the present invention found that the main causes (inability to obtain a spherical expanded slag with few surface pores) are the control of slag temperature, viscosity, slag flow rate, flow shape control, and I learned that there were problems with the control of water volume and the method of dispersing water over long distances.

本発明は上述の問題点を解決し、表面気孔の少い球形の
膨張スラグを製造する方法並びに装置に係るもので、そ
の要旨は、高炉溶滓を、水槽内に縦方向に挿置され周側
壁に複数個の水流人孔が貫設された湾曲状樋の上部開口
部から流入し、大気中に開放された湾曲状樋の下部開口
部に於いて上記高炉溶滓を大気中に強制飛散せしめるこ
とを特徴とする球形膨張スラグの製造方法、並びに水槽
内に、周側壁に複数個の水流人孔が貫設された湾曲状樋
を縦方向に挿置し、該湾曲状樋の上部開口部は前記水槽
と隣接された高炉溶滓受ホッパーより突設された水平樋
と連通され、一方下部開口部は大気中に開放された状態
とされており、かつ湾曲状樋の下部開口部近くに高炉溶
滓飛散用の送風機を配設したことを特徴とする球形膨張
スラグの製造装置である。
The present invention solves the above-mentioned problems and relates to a method and apparatus for manufacturing spherical expanded slag with few surface pores. The blast furnace slag flows into the upper opening of the curved gutter, which has multiple water holes in the side wall, and is forcibly dispersed into the atmosphere at the lower opening of the curved gutter, which is open to the atmosphere. A method for producing a spherical expanded slag characterized by: vertically inserting a curved gutter having a plurality of water flow holes through the circumferential side wall in a water tank, and an upper opening of the curved gutter. The lower part communicates with a horizontal gutter protruding from the blast furnace slag receiving hopper adjacent to the water tank, while the lower opening is open to the atmosphere, and the lower opening of the curved gutter is connected to the horizontal gutter. This is an apparatus for manufacturing spherical expanded slag, characterized in that a blower for scattering blast furnace slag is installed in the slag.

以下、本発明を図面に示す実施例について説明する。Embodiments of the present invention shown in the drawings will be described below.

図面に於いて1は溶滓鍋、2は溶滓受ホツパ−,3はホ
ッパーの流出口、4は流出口に設けられた流出量調整ダ
ンパー、5は流出口に続いて流出口の中具より大きい中
具の水平樋、6はこの水平樋の先端付近に設けた流量(
厚)調整板、7は複数の水流人孔8を有する綾状の湾曲
状樋、9は上部開口部、10は下部開口部、11は水槽
、12は蒸気筒、13は給水管、14は遠心送風装置、
15は遠心送風機、16は搬出コンベア、17は排水溝
、18は飛散室、19は換気装置、20は流量(厚)調
整板固定用孔、21は同差込ピン、22はキャスター、
23は溶滓を示す。
In the drawing, 1 is a slag ladle, 2 is a slag receiving hopper, 3 is an outlet of the hopper, 4 is an outflow adjustment damper provided at the outlet, and 5 is a fitting for the outlet following the outlet. The larger horizontal gutter, 6, is the flow rate installed near the tip of this horizontal gutter (
7 is a curved gutter having a plurality of water flow holes 8, 9 is an upper opening, 10 is a lower opening, 11 is a water tank, 12 is a steam cylinder, 13 is a water supply pipe, 14 is a centrifugal blower,
15 is a centrifugal blower, 16 is an unloading conveyor, 17 is a drain, 18 is a scattering chamber, 19 is a ventilation device, 20 is a hole for fixing a flow rate (thickness) adjustment plate, 21 is an insertion pin, 22 is a caster,
23 indicates slag.

以上の構成であるから、溶滓鍋等かう流下する溶滓の流
量、流速、流形等を調整する受払ホッパー2を溶滓鍋等
と近接して設けると共に、このホッパーの流出口3には
、ホッパー2から流出する溶滓の流量、流速、流形等を
調整する流出量調整ダンパー4を設ける。
With the above configuration, the receiving and discharging hopper 2 for adjusting the flow rate, flow velocity, flow shape, etc. of the flowing slag, such as the slag ladle, is provided close to the slag ladle, etc., and the outlet 3 of this hopper is provided. An outflow adjustment damper 4 is provided to adjust the flow rate, flow velocity, flow shape, etc. of the slag flowing out from the hopper 2.

又ホッパー流出口3に続いてホッパーから流出した溶滓
の流速の緩和と流量を薄状にするため流出口中具より大
きい中具の水平樋5を設けると共に、この水平樋の先端
には綾状の湾曲状樋7への流下厚を調整する流量(厚)
調整板6を設ける。
Further, following the hopper outlet 3, a horizontal gutter 5 with a larger inner fitting than the outlet is provided in order to moderate the flow velocity of the slag flowing out from the hopper and make the flow rate thinner, and a twill-shaped groove is provided at the tip of this horizontal gutter. Flow rate (thickness) that adjusts the thickness of the flow into the curved gutter 7
An adjustment plate 6 is provided.

以上によって、溶滓鍋等から流下した溶滓は、一定の流
量、流速、及び流形に調整されて綾状の湾曲状樋7に流
入し樋を流下中に後述の方法によって、所定温度に冷却
されるものである。
As described above, the molten slag flowing down from the slag pot etc. is adjusted to a constant flow rate, flow rate, and flow shape, and flows into the twilled curved gutter 7, and is heated to a predetermined temperature by the method described later while flowing down the gutter. It is something that is cooled.

なお、この樋の口径形状は溶滓流形と同じくすることが
好ましく、縦の形状は、溶滓の流下厚が小さい場合は第
5図のように、一部を垂直にするだけでよいが、溶滓流
玉量が大きい場合は第1図のようにくねりをもたせるこ
とが溶滓の表裏を均等に冷却できるという点から好まし
い。
The diameter of this gutter is preferably the same as the slag flow shape, and if the thickness of the slag flowing down is small, it is sufficient to make only a part of the vertical shape vertical, as shown in Figure 5. When the amount of molten slag is large, it is preferable to have a bend as shown in FIG. 1, since the front and back sides of the slag can be cooled evenly.

又、この湾曲状樋には複数の水流人孔8を設ける。Further, a plurality of water holes 8 are provided in this curved gutter.

この水流人孔は樋に流入する時点(付近)の溶滓熱含量
を、樋から流出する時点に於いて最大に膨張し、但し分
散と同時に表面張力が働いて球形を作るに必要な最小限
度の醜態熱含量(以下最小限度の醜態熱含量という)に
するため、必要な水量が流入するように設けられる。
This water hole expands the heat content of the slag at (near) the time it flows into the gutter to the maximum at the time it flows out from the gutter, but at the same time as dispersion, surface tension acts to the minimum level necessary to form a spherical shape. It is provided so that the necessary amount of water flows in order to maintain the abominable heat content (hereinafter referred to as the minimum abominable heat content).

又、水流人孔はできるだけ小さく、孔数が多くなるよう
に設けることが好ましく、更に樋の口径は下方に行くに
従い、大きくすると共に、水槽の大きさは所要水量、所
要流速(溶滓落下流速に等しくする)との関連で決める
ことが好ましい。
In addition, it is preferable to make the water flow holes as small as possible and to increase the number of holes.Furthermore, the diameter of the gutter should be increased as it goes downward, and the size of the water tank should be determined based on the required water volume and required flow rate (depending on the slag falling flow rate). It is preferable to decide in relation to (make them equal).

なお、最小限度の醜態熱含量は、例えば流入溶滓の熱含
量を予め実績温度、比熱から設定し、この熱含量を最小
限度の醜態熱含量にする必要な水量を決め、次いで実際
に流入する溶滓の熱含量が設定した熱含量と異なる場合
は、6の流量(厚)調整板を操作して、溶滓流量を調整
すれば水量を変更することなく、はぼ一定にすることが
できるものである。
The minimum amount of heat content can be determined by, for example, setting the heat content of the inflowing slag in advance from the actual temperature and specific heat, determining the amount of water required to make this heat content the minimum amount of heat content, and then determining the amount of water that actually flows into the slag. If the heat content of the slag is different from the set heat content, you can adjust the flow rate of the slag by operating the flow rate (thickness) adjustment plate 6 to keep it almost constant without changing the water volume. It is something.

又、最小限度の醜態熱含量にするに必要な水量は実際の
蒸気発生量や使用前後の水の温度或いは樋流下中の放散
熱量等をつかんでから、設定する必要のあることはいう
までもない。
It goes without saying that the amount of water required to achieve the minimum amount of heat content must be set after determining the actual amount of steam generated, the temperature of the water before and after use, the amount of heat dissipated in the flow down the gutter, etc. do not have.

以上のようにして湾曲状樋に流入した溶滓は一定の間隔
をおいて設けられた複数の流入孔8から所要水量の噴射
を受けながら、流下し、最小限度の醜態熱含量を残して
下部開口部10に至り、その下方に設けた14の遠心送
風装置によって空中に粒状となって飛散し、表面張力に
よって球形を作って固化しなから16の搬出ベルトに乗
り、所定置場に搬送されるものである。
The molten slag that has flowed into the curved gutter as described above flows down while being sprayed with the required amount of water from the plurality of inlet holes 8 provided at regular intervals, leaving a minimum amount of heat content in the lower part. The particles reach the opening 10, are dispersed into particles in the air by the centrifugal blower 14 installed below, solidify into a spherical shape due to surface tension, and then ride the 16 delivery belts and are transported to a predetermined location. It is something.

この場合、重要なのは、飛散粒滓の空中にある時間が短
かいと、表面張力の作用する時間も短かくなって、球形
を作ることが困難となり、再融着することにもなるので
、できるだけ長く空中にあるような送風角度を設定する
ことである。
In this case, the important thing is that if the time that the scattered particles remain in the air is short, the time for surface tension to act is also short, making it difficult to form a spherical shape and causing re-fusion. The idea is to set the angle of the air so that it stays in the air for a long time.

この角度は下限は水平方向、上限は水平に対し21°の
方向、即ちこの上限と下限との範囲に調節すれば得られ
るが、飛散室の大きさ及び飛散室の据え方、位置などに
よって異なる。
This angle can be obtained by adjusting the lower limit to the horizontal direction and the upper limit to the direction of 21 degrees to the horizontal, that is, by adjusting the range between the upper limit and the lower limit, but it will vary depending on the size of the scattering chamber, how the scattering chamber is installed, the position, etc. .

以上述べて来た様に、本願発明方法によれば、水槽内に
ある高炉溶滓流下用の樋を縦方向に挿置し、しかも該樋
は湾曲状であり、かつ樋の周側壁には多数の水流人孔が
貫設されているので、中を流下する高炉溶滓は全体的に
均等に冷却をする事が可能で軽くて表面気孔の少い球形
の膨張スラグを造ることが出来る。
As described above, according to the method of the present invention, a gutter for flowing down blast furnace slag in a water tank is inserted vertically, and the gutter is curved, and the circumferential side wall of the gutter is Since many water holes are installed through the blast furnace, the blast furnace slag flowing down can be cooled evenly throughout, making it possible to create a light, spherical expanded slag with few surface pores.

又本願発明装置は上述の膨張スラグの製造を効率よく、
かつ安全に行うことが出来るものである。
In addition, the device of the present invention can efficiently produce the above-mentioned expanded slag.
And it can be done safely.

以下実施例を述べる。Examples will be described below.

実施例 本実施例に使用した原料は次の組成を有する高炉滓であ
る。
Example The raw material used in this example was blast furnace slag having the following composition.

この高炉滓を大体第1図と同じ構造を有する装置を用い
、但し、溶滓受ホッパーの流出口の口径は150%×1
00%、流出量調整ダンパー4の使用により、流出口の
口径は50%×60%、これに接続する水平樋5は長さ
600%、巾250%、但し、この水平樋内にはキャス
ターを塗布すると共に、凸部を設けて、一旦停りながら
拡がって、ゆっくり流れるようにした溶滓の実際流出中
は約200%、流量(厚)調整板6は流量厚15%で調
整、綾状樋7の流入口の口径は250%×100%で、
流入口から300%以下付近から250%×125〜2
00%に漸次拡げる。
This blast furnace slag is collected using a device having roughly the same structure as shown in Figure 1, except that the diameter of the outlet of the slag receiving hopper is 150% x 1.
00%, by using the outflow adjustment damper 4, the diameter of the outflow port is 50% x 60%, and the horizontal gutter 5 connected to this is 600% long and 250% wide, however, casters are not installed in this horizontal gutter. At the same time as coating, a convex part is provided so that the slag spreads while stopping and flows slowly.The actual flow rate of the slag is approximately 200%, and the flow rate (thickness) adjustment plate 6 is adjusted to a flow rate thickness of 15%. The diameter of the inlet of gutter 7 is 250% x 100%,
250% x 125~2 from around 300% or less from the inlet
Gradually expand to 00%.

長さは約1250%、曲り角度は水平に対し40°、噴
射角度は同水平に対して20°、8の水流出孔の断面径
及び孔数は上段13%26コ1.中段7%26コ、下段
5%26つ、使用水の温度21℃、使用水量は溶滓温度
1350℃(熱含量367騙/IKg)トン当り0.7
93m3、溶滓流量約30トン/Hの条件で遠心送風機
は風量600 rr?/分、圧力250 % Agを使
用した。
The length is approximately 1250%, the bending angle is 40° to the horizontal, the injection angle is 20° to the horizontal, the cross-sectional diameter of the water outlet hole 8 and the number of holes are 13% in the upper row. Middle row 7% 26 pieces, lower row 5% 26 pieces, temperature of water used is 21℃, amount of water used is slag temperature 1350℃ (heat content 367cm/IKg) 0.7 per ton
The centrifugal blower has an air volume of 600 rr under conditions of 93 m3 and a slag flow rate of approximately 30 tons/h? /min, pressure 250% Ag was used.

この条件下で生成したスラグは表面気孔率の少い殆んど
球形の膨張スラグで、粒度は15%以上が0.5〜2.
4%、15%以下5%以上が10.2〜16.3%、5
%以下81〜89チ、絶乾比重は1.45〜1.6、容
量は粗骨材(15%〜5%)が0.75〜0.80、細
骨材(5%以下)が1.0〜1.09、実績率50係以
上で、膨張しないスラグや球形の不完全な膨張スラグは
無視し得る程度に少かった。
The slag produced under this condition is an almost spherical expanded slag with low surface porosity, and the particle size is 0.5 to 2.5% with a particle size of 15% or more.
4%, 15% or less, 5% or more is 10.2-16.3%, 5
% or less, 81 to 89 inches, absolute dry specific gravity 1.45 to 1.6, capacity 0.75 to 0.80 for coarse aggregate (15% to 5%), and 1 for fine aggregate (5% or less). .0 to 1.09, and the performance rate was 50 or higher, and the number of unexpanded slags and incompletely expanded slags of spherical shape was negligible.

以上の様に、本願発明によれば、軽くて表面気孔の少い
球形の膨張スラグか得られるので、軽量骨材としてコン
クリ−ドブ泊ツク、高層建築の構造用コンクリート骨材
、その他絶縁材、路盤材等に有効利用し得る。
As described above, according to the present invention, a spherical expanded slag that is light and has few surface pores can be obtained, so that it can be used as a lightweight aggregate for concrete slabs, structural concrete aggregates for high-rise buildings, and other insulating materials. It can be effectively used for roadbed materials, etc.

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

第1図は本発明装置の平面図、第2図は第1図A−A線
に於ける断面図、第3図は水平樋部分の拡大平面図、第
4図は水平樋及び湾曲状樋部分の一部切欠説明図、第5
図は湾曲状樋の一部を垂直にした場合の一部切欠説明図
。 図中、1・・・・・・溶滓鍋、2・・・・・・溶滓受ホ
ツパ−。 3・・・・・・ホッパー流出口、4・・・・・・流出量
調整ダンパー、5・・・・・・水平樋、6・・・・・・
流量(厚)調整板、7・・・・・・湾曲状樋、8・・・
・・・水流人孔、9・・・・・・上部開口部、10・・
・・・・下部開口部、11・・・・・・水槽、12・・
・・・・蒸気筒、13・・・・・・給水管、14・・・
・・・遠心送風装置、15・・・・・・遠心送風機、1
6・・・・・・搬出コンベア、17・・・・・・排水管
、18・・・・・・飛散室、19・・・・・・換気装置
Fig. 1 is a plan view of the device of the present invention, Fig. 2 is a sectional view taken along line A-A in Fig. 1, Fig. 3 is an enlarged plan view of the horizontal gutter portion, and Fig. 4 is a horizontal gutter and a curved gutter. Partial cutaway explanatory diagram of the part, No. 5
The figure is a partially cutaway explanatory diagram when a part of the curved gutter is made vertical. In the figure, 1... slag pot, 2... slag receiving hopper. 3...Hopper outlet, 4...Outflow adjustment damper, 5...Horizontal gutter, 6...
Flow rate (thickness) adjustment plate, 7... Curved gutter, 8...
...Water hole, 9...Top opening, 10...
... lower opening, 11 ... water tank, 12 ...
...Steam cylinder, 13...Water supply pipe, 14...
... Centrifugal blower, 15 ... Centrifugal blower, 1
6... Carrying out conveyor, 17... Drain pipe, 18... Scattering room, 19... Ventilation device.

Claims (1)

【特許請求の範囲】 1 高炉溶滓を、水槽内に縦方向に挿置され周側壁に複
数個の水流人孔が貫設された湾曲状樋の上部開口部から
流入し、大気中に開放された湾曲状樋の下部開口部に於
いて上記高炉溶滓を大気中に強制飛散せしめることを特
徴とする球形膨張スラグの製造方法。 2 水槽内に、周側壁に複数個の水流人孔が貫設された
湾曲状樋を縦方向に挿置し、該湾曲状樋の上部開口部は
前記水槽と隣設された高炉溶滓受ホッパーより突設され
た水平樋と連通され、一方、下部開口部は大気中に開放
された状態とされており、かつ湾曲状樋の下部開口部近
くに高炉溶滓飛散用の送風機を配設したことを特徴とす
る球形膨張スラグの製造装置。
[Scope of Claims] 1. Blast furnace slag flows into the upper opening of a curved gutter that is vertically inserted into a water tank and has a plurality of water flow holes through the circumferential side wall, and is released to the atmosphere. A method for producing spherical expanded slag, characterized in that the blast furnace slag is forcibly scattered into the atmosphere at a lower opening of a curved gutter. 2 A curved gutter with a plurality of water holes penetrating the circumferential wall is vertically inserted into the water tank, and the upper opening of the curved gutter is connected to the blast furnace slag receiver installed adjacent to the water tank. It communicates with a horizontal gutter that protrudes from the hopper, while the lower opening is open to the atmosphere, and a blower for scattering blast furnace slag is installed near the lower opening of the curved gutter. An apparatus for manufacturing spherical expanded slag, which is characterized by:
JP55047229A 1980-04-10 1980-04-10 Method and device for producing spherical expanded slag Expired JPS591227B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55047229A JPS591227B2 (en) 1980-04-10 1980-04-10 Method and device for producing spherical expanded slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55047229A JPS591227B2 (en) 1980-04-10 1980-04-10 Method and device for producing spherical expanded slag

Publications (2)

Publication Number Publication Date
JPS56142806A JPS56142806A (en) 1981-11-07
JPS591227B2 true JPS591227B2 (en) 1984-01-11

Family

ID=12769368

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55047229A Expired JPS591227B2 (en) 1980-04-10 1980-04-10 Method and device for producing spherical expanded slag

Country Status (1)

Country Link
JP (1) JPS591227B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT405511B (en) * 1997-10-29 1999-09-27 Holderbank Financ Glarus METHOD FOR GRANULATING AND CRUSHING MELT LIQUID MATERIAL, AND DEVICE FOR CARRYING OUT THIS METHOD

Also Published As

Publication number Publication date
JPS56142806A (en) 1981-11-07

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