JPS581052B2 - Mining slag fragmentation and heat recovery method - Google Patents

Mining slag fragmentation and heat recovery method

Info

Publication number
JPS581052B2
JPS581052B2 JP51134293A JP13429376A JPS581052B2 JP S581052 B2 JPS581052 B2 JP S581052B2 JP 51134293 A JP51134293 A JP 51134293A JP 13429376 A JP13429376 A JP 13429376A JP S581052 B2 JPS581052 B2 JP S581052B2
Authority
JP
Japan
Prior art keywords
slag
fibers
cooling tower
heat recovery
fragmentation
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
JP51134293A
Other languages
Japanese (ja)
Other versions
JPS5361725A (en
Inventor
西岡和正
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP51134293A priority Critical patent/JPS581052B2/en
Publication of JPS5361725A publication Critical patent/JPS5361725A/en
Publication of JPS581052B2 publication Critical patent/JPS581052B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • C03B37/01Manufacture of glass fibres or filaments
    • C03B37/02Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
    • 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
    • C21B2400/05Apparatus features
    • C21B2400/066Receptacle features where the slag is treated
    • C21B2400/074Tower structures for cooling, being confined but not sealed
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/08Treatment of slags originating from iron or steel processes with energy recovery

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)
  • Glass Compositions (AREA)
  • Manufacture Of Iron (AREA)

Description

【発明の詳細な説明】 本発明は鉱滓の細分化・熱回収方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for fragmenting slag and recovering heat.

一般に、溶鉱炉において銑鉄を製造する場合、鉱石の溶
融時における溶剤の作用によりスラグと呼ばれる鉱滓が
生じ、この鉱滓は銑鉄とは別に溶鉱炉から取り出さなけ
ればならず、その処理が1つの大きな問題となっている
Generally, when producing pig iron in a blast furnace, slag called slag is produced due to the action of a solvent when ore is melted, and this slag must be taken out of the blast furnace separately from the pig iron, and its disposal is a major problem. ing.

従来は、第4図に示すように、溶鉱炉41内の底部にお
いて銑鉄42の上方にたまった鉱滓43は矢印44で示
す如く溶融状態のまま別の容器45の中に取り出して自
然放冷させるか、あるいは特に処理を施すことなく水中
に投入して冷却させたりしていたので、冷却により凝固
した鉱滓は大きな塊となり、その後の再利用または廃棄
処理等の取扱いに多犬な労力を要し、処理作業に非常な
困難を来たす他、その水の汚染を生じていた。
Conventionally, as shown in FIG. 4, slag 43 accumulated above pig iron 42 at the bottom of a blast furnace 41 is taken out in a molten state as shown by arrow 44 into another container 45 and allowed to cool naturally. Otherwise, the slag was put into water and cooled without any special treatment, so the slag solidified by cooling and became large lumps, which required a lot of effort to handle for subsequent reuse or disposal. In addition to making treatment work extremely difficult, the water was also contaminated.

また、このような従来法では、溶融鉱滓の持つ莫大な高
熱の回収も有効に行なうことができず、そのまま無駄に
なってしまっていた。
Further, in such conventional methods, the extremely high heat contained in the molten slag cannot be effectively recovered, and the slag is wasted.

本発明は上記従来技術の欠点を解消するためになされた
もので、鉱滓を繊維状で回収することにより、その後の
再利用、投棄等の取扱いを極めて簡単かつ容易にすると
共に、鉱滓中の熱も有効に回収できる鉱滓の細分化・熱
回収方法を提供することを目的とするものである。
The present invention has been made to solve the above-mentioned drawbacks of the prior art, and by recovering slag in the form of fibers, handling such as subsequent reuse and dumping becomes extremely simple and easy. The purpose of this invention is to provide a method for fragmentation and heat recovery of slag that can effectively recover slag.

この目的を達成するため、本発明の方法は、鉱滓を溶鉱
炉から冷却塔内に放出する際に細分化装置により直接溶
融状態で細分化または繊維化し、それを冷却塔内で冷媒
により冷却凝固させ、細滓または滓繊維として回収する
と共に、冷媒は熱回収後、適当な熱回収装置に導くよう
にしたことを特徴とする。
In order to achieve this objective, the method of the present invention involves directly fragmenting or fiberizing the slag in a molten state using a fragmentation device when it is discharged from a blast furnace into a cooling tower, and solidifying it by cooling with a refrigerant in the cooling tower. The refrigerant is characterized in that it is recovered as fine slag or slag fibers, and that the refrigerant is guided to a suitable heat recovery device after heat recovery.

以下、添付図面に即して本発明をさらに説明する。The present invention will be further described below with reference to the accompanying drawings.

第1図は本発明に用いる装置の一例を示す概略系統図で
ある。
FIG. 1 is a schematic system diagram showing an example of a device used in the present invention.

溶鉱炉1の底部には溶銑2が形成され、この溶銑2の上
方には溶融状態の鉱滓3が形成されている。
Hot metal 2 is formed at the bottom of the blast furnace 1, and molten slag 3 is formed above the hot metal 2.

溶銑2は取出管4で取り出され、鉱滓3はこれとは別に
排出管5を通って排出される。
The hot metal 2 is taken out through a take-off pipe 4, and the slag 3 is separately discharged through a discharge pipe 5.

排出管5から排出された鉱滓3は冷却塔8内に送り込ま
れるが、排出管5の先端部には、鉱滓3を繊維状に細分
化し、細滓または滓繊維9として冷却塔8内に放出する
ための細分化装置6が設けられており、鉱滓3は溶融状
態で重力によりこの細分化装置6の細分化ノズル7を通
って冷却塔8内に放出される。
The slag 3 discharged from the discharge pipe 5 is sent into the cooling tower 8. At the tip of the discharge pipe 5, the slag 3 is finely divided into fibers and discharged into the cooling tower 8 as fine slag or slag fibers 9. The slag 3 is discharged in a molten state by gravity through a fragmentation nozzle 7 of this fragmentation device 6 into a cooling tower 8.

本実施例の細分化装置6は第2図に拡大して示すように
ほぼ三角形状の縦断面形状を有している。
The subdivision device 6 of this embodiment has a substantially triangular longitudinal cross-sectional shape, as shown in an enlarged view in FIG.

冷却塔8はその最下部に、冷媒である空気10の取入口
と、細分化された細滓または滓繊維9の回収用の出口と
を兼ねる開口11を有し、一方上端には、細滓または滓
繊維9との接触により熱を吸収して高温になった空気1
0をたとえばボイラの如き熱回収装置(図示せず)に導
ひくため排出口12が設けられている。
The cooling tower 8 has an opening 11 at its lowest part that serves as an inlet for air 10, which is a refrigerant, and an outlet for recovering the finely divided slag or slag fibers 9. Or the air 1 that has become high temperature by absorbing heat due to contact with the slag fibers 9
An outlet 12 is provided for conducting the 0 to a heat recovery device (not shown), such as a boiler.

次に、本発明による作用につき説明するに、まず溶鉱炉
1内の鉱滓3を排出管5により溶融状態のまま冷却塔8
内の細分化装置6に導びさ、この細分化装置6の細分化
ノズル7から重力により直接冷却器8の中に放出して細
滓または滓繊維9を形成し、冷却器8内を下降させる。
Next, to explain the operation of the present invention, first, the slag 3 in the blast furnace 1 is transferred to the cooling tower 3 while being molten through the discharge pipe 5.
The slag or slag fibers 9 are discharged directly into the cooler 8 by gravity from the fragmentation nozzle 7 of the fragmenter 6 to form fine slag or slag fibers 9, which are then lowered through the cooler 8. .

一方、細滓または滓繊維9を冷却して熱回収を行なう空
気10は冷却塔8の開口11から導入されて冷却塔8内
を上昇するが、その際上記の如くして形成された溶融状
態の細滓または滓繊維9と接触し、熱を吸収して冷却し
、繊維状のままで次第に凝固させる。
On the other hand, air 10 for cooling the fine slag or slag fibers 9 and recovering heat is introduced from the opening 11 of the cooling tower 8 and rises inside the cooling tower 8, but at this time, the molten state formed as described above is It comes into contact with the fine slag or slag fibers 9, absorbs heat, cools it, and gradually solidifies while remaining fibrous.

それにより、細滓または滓繊維9は粘着力を失なった状
態で第1図に矢印9aで示すように開口11から回収さ
れ、廃棄または再利用されるが、再利用の場合には用途
に見合うように適度に圧縮して岩綿繊維の保温材等への
利用が可能であり、また廃棄の場合でもそれに適するよ
うに容易に粉砕して埋立その他の廃棄処理をすることが
できる。
As a result, the fine slag or slag fibers 9 are collected from the opening 11 as shown by the arrow 9a in FIG. 1 in a state where they have lost their adhesive strength, and are discarded or reused. It is possible to use the rock wool fibers as heat insulating materials by compressing them appropriately, and even when discarding them, they can be easily crushed and disposed of in landfills or other forms of disposal.

細滓または滓繊維9から熱を吸収した空気10はたとえ
ば1000℃にまで高温化し、排出口12を通って熱回
収装置に導ひかれるが、高温の熱源としてボイラ等のた
めに有効に再利用できる。
The air 10 that has absorbed heat from the slag or slag fibers 9 is heated to a temperature of, for example, 1000° C., and is led to a heat recovery device through an outlet 12, where it can be effectively reused as a high-temperature heat source for a boiler or the like. can.

第3図は細分化装置の変形例を示し、この細分化装置6
aはほぼ半円形の縦断面形状を有し、細分化ノズル7a
は放射状に多数配置されているので、冷却塔8の内部全
体に細滓または滓繊維9aを形成できるという利点があ
る。
FIG. 3 shows a modification of the subdivision device, and this subdivision device 6
a has a substantially semicircular vertical cross-sectional shape, and the subdividing nozzle 7a
Since a large number of slags or slag fibers 9a are arranged radially, there is an advantage that fine slag or slag fibers 9a can be formed throughout the inside of the cooling tower 8.

以上説明したように、本発明によれば、鉱滓を繊維状に
分細化および凝固させて回収することにより、その後の
再利用や投棄等の取扱いが極めて容易で、省力化が図ら
れると同時に、この繊維状の鉱滓からの熱の吸収も極め
て効率的になされ、熱の回収および再利用が非常に有効
に行なわれる。
As explained above, according to the present invention, by dividing and solidifying the slag into fibers and recovering it, subsequent handling such as reuse and dumping is extremely easy, and labor-saving is achieved. The absorption of heat from this fibrous slag is also extremely efficient, and the recovery and reuse of heat is very effective.

また、本発明に用いる冷媒である空気は溶滓からの積極
的な不純物の溶解を生じることがなく、冷媒の処理は不
要であり、従来の水中投棄法のように溶滓中の成分の溶
解により水中に不純物が混入し、その水を排出前に処理
することが必要となる等の不便かつ無駄な作業は生じる
余地がなく、極めて有利である。
In addition, air, which is the refrigerant used in the present invention, does not actively dissolve impurities from the slag, and there is no need to treat the refrigerant. This is extremely advantageous because there is no room for inconvenient and wasteful operations such as impurities being mixed into the water and the water having to be treated before being discharged.

さらに、本発明においては、鉱滓が冷却塔内を重力によ
り下降し、一方、冷媒である空気が自然対流により上昇
して、これらが向流接触することによって鉱滓の冷却凝
固が行なわれるのであるから、鉱滓の細分化を行なって
細滓または滓繊維となすに際して別に動力を必要としな
いという利点がある。
Furthermore, in the present invention, the slag descends in the cooling tower by gravity, while the air, which is a refrigerant, rises by natural convection, and the slag is cooled and solidified by countercurrent contact. This method has the advantage that no separate power is required to fragment the slag into fine slag or slag fibers.

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

第1図は本発明に用いる装置の一例を示す概略系統図、
第2図は細分化装置の拡大縦断面図、第3図は細分化装
置の一変形例の拡大縦断面図、第4図は従来技術を示す
説明図である。 1……溶鉱炉、2……溶銑、3……鉱滓、5……排出管
、6,6a……細分化装置、7,7a……細分化ノズル
、8……冷却塔、9,9a……紙滓または滓繊維、10
……空気。
FIG. 1 is a schematic system diagram showing an example of a device used in the present invention;
FIG. 2 is an enlarged vertical sectional view of a fragmentation device, FIG. 3 is an enlarged vertical sectional view of a modified example of the fragmentation device, and FIG. 4 is an explanatory diagram showing a conventional technique. 1... Blast furnace, 2... Hot metal, 3... Slag, 5... Discharge pipe, 6, 6a... Refinement device, 7, 7a... Refinement nozzle, 8... Cooling tower, 9, 9a... Slag paper or slag fiber, 10
……air.

Claims (1)

【特許請求の範囲】[Claims] 1 溶鉱炉内の鉱滓を、細分化ノズルを介して溶融状態
で重力により冷却塔内に繊維状に細分化して放出して該
冷却塔内を下降させ、それを冷却塔内で上昇する空気に
向流接触させることにより冷却凝固させ、細滓または滓
繊維として回収すると共に、前記接触によって加熱され
た空気から熱回収を行なうことを特徴とする鉱滓の細分
化・熱回収方法。
1 The slag in the blast furnace is finely divided into fibers in a molten state by gravity and discharged into the cooling tower through a fragmentation nozzle, and is lowered in the cooling tower, and is directed toward the rising air in the cooling tower. A method for fragmentation and heat recovery of slag, which comprises cooling and solidifying the slag by bringing it into contact with a flow, recovering it as fine slag or slag fibers, and recovering heat from the air heated by the contact.
JP51134293A 1976-11-09 1976-11-09 Mining slag fragmentation and heat recovery method Expired JPS581052B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51134293A JPS581052B2 (en) 1976-11-09 1976-11-09 Mining slag fragmentation and heat recovery method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51134293A JPS581052B2 (en) 1976-11-09 1976-11-09 Mining slag fragmentation and heat recovery method

Publications (2)

Publication Number Publication Date
JPS5361725A JPS5361725A (en) 1978-06-02
JPS581052B2 true JPS581052B2 (en) 1983-01-10

Family

ID=15124888

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51134293A Expired JPS581052B2 (en) 1976-11-09 1976-11-09 Mining slag fragmentation and heat recovery method

Country Status (1)

Country Link
JP (1) JPS581052B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5076328A (en) * 1973-10-10 1975-06-23

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5076328A (en) * 1973-10-10 1975-06-23

Also Published As

Publication number Publication date
JPS5361725A (en) 1978-06-02

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