JPS5835943B2 - Granulation method of molten blast furnace slag - Google Patents

Granulation method of molten blast furnace slag

Info

Publication number
JPS5835943B2
JPS5835943B2 JP9979676A JP9979676A JPS5835943B2 JP S5835943 B2 JPS5835943 B2 JP S5835943B2 JP 9979676 A JP9979676 A JP 9979676A JP 9979676 A JP9979676 A JP 9979676A JP S5835943 B2 JPS5835943 B2 JP S5835943B2
Authority
JP
Japan
Prior art keywords
blast furnace
furnace slag
slag
molten
container
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
JP9979676A
Other languages
Japanese (ja)
Other versions
JPS5325643A (en
Inventor
真弓 吉永
弘 山岡
達彦 重松
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 Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP9979676A priority Critical patent/JPS5835943B2/en
Publication of JPS5325643A publication Critical patent/JPS5325643A/en
Publication of JPS5835943B2 publication Critical patent/JPS5835943B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Manufacture Of Iron (AREA)
  • Glanulating (AREA)

Description

【発明の詳細な説明】 この発明は高炉から排出された溶滓を減圧容器を使って
粒状化処理する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for granulating slag discharged from a blast furnace using a vacuum vessel.

近年、高炉の大型化に伴ない、高炉から排出される溶滓
も膨大な量に達し、これを資源化して有効に利用するこ
とは工業的に極めて右益である。
In recent years, with the increase in the size of blast furnaces, the amount of slag discharged from the blast furnaces has also reached an enormous amount, and it is of great industrial benefit to turn this into a resource and use it effectively.

従来実施されている高炉滓の有効利用方法としては、主
に高炉滓を粒状化してコンクリート等の骨材に利用する
方法が代表的であり、その粒状化する方法には高圧水吹
付法(水滓)、あるいは回転体への衝突による飛散、さ
らには噴霧法等が採用されている。
A typical method of effectively utilizing blast furnace slag that has been practiced in the past is to granulate it and use it as aggregate for concrete, etc. Slag), scattering by collision with a rotating body, and even spraying methods are employed.

しかし、これらの方法はいずれも冷却過程において発泡
し、気孔が多く発生することから粒状化された高炉滓は
強度的に弱い面があり、また処理するのに必要な設備の
しめる面積も大であるという欠点があった。
However, in all of these methods, the granulated blast furnace slag is weak in strength because it foams during the cooling process and many pores are generated, and the equipment required to process it requires a large area. There was a drawback.

この発明者らは、研究を重ねた結果、高炉滓にはN2
、N2 、COの成分が多量に含まれているという事実
と、これらの成分は真空中においてガス化するという、
この二つの事実に基づいて発明を完成したものであるっ つまり、N2 、N2 、CO酸成分含有する高炉滓を
減圧した容器内に流下すれば、これらの成分はガスとな
り溶滓中より放出し、同時に溶滓が分散して粒状化され
るのである。
As a result of repeated research, the inventors found that blast furnace slag contains N2.
, N2, and CO are contained in large amounts, and that these components gasify in a vacuum.
The invention was completed based on these two facts. In other words, if blast furnace slag containing N2, N2, and CO acid components flows into a depressurized container, these components become gas and are released from the slag. At the same time, the slag is dispersed and granulated.

この粒状化に必要な真空度は、実験室的に行った結果を
示す第2図から200miHg以下に限定することが望
ましい。
The degree of vacuum required for this granulation is desirably limited to 200 miHg or less, as shown in FIG. 2, which shows the results obtained in a laboratory.

この方法により造粒された粒状化物は脱ガスされている
ので、冷却速度にかかわりなく稠密なものとなる。
Since the granulated product granulated by this method is degassed, it becomes dense regardless of the cooling rate.

一方、溶融高炉滓を減圧容器内に流下する前に水蒸気、
窒素等を吹き込み処理すれば、内部は発泡し軽量骨材の
製造も可能である。
On the other hand, before the molten blast furnace slag flows down into the reduced pressure vessel, steam
If nitrogen or the like is blown into the material, the inside will foam and lightweight aggregates can be produced.

次に、この発明法を実施するための装置について説明す
る。
Next, an apparatus for carrying out this invention method will be explained.

第1図はその装置の一例を示すもので、1は減圧容器、
2はトラフ、3は」閉板、4はシュート、5は搬出用ス
クリュウコンベヤー、6は搬送用ベルトコンベヤーであ
る。
Figure 1 shows an example of the device, where 1 is a vacuum vessel;
2 is a trough, 3 is a closing plate, 4 is a chute, 5 is a screw conveyor for carrying out, and 6 is a belt conveyor for conveyance.

すなわち、高炉から排出された溶滓は溶滓樋または溶滓
鍋を介してシュート4より流量を調整されてトラフ2に
導入され、開閉板3を通過して減圧容器1内に流下され
る。
That is, the molten slag discharged from the blast furnace is introduced into the trough 2 through the chute 4 via the slag gutter or the slag ladle, with its flow rate being adjusted, and is allowed to flow down into the reduced pressure vessel 1 through the opening/closing plate 3.

開閉板3はAl板、Cu板等の低融点金属板を使用する
The opening/closing plate 3 uses a low melting point metal plate such as an Al plate or a Cu plate.

造粒作業開始時容器内を減圧する場合トラフと容器の間
に設置して容器を密閉する目的で使用するもので、容器
内0減圧が完了した後溶滓をトラフ2内に流入すれ:f
開閉板が溶解され減圧された容器内に溶滓が流下し始め
造粒されその後の減圧状態はスチームエジェクター9に
より維持される減圧容器1に高炉滓が流下されると、高
炉滓中に含有されているN2 、N2 、COの各成分
は低気圧にさらされることによりガスとなって溶滓中よ
り放出される。
When the pressure inside the container is reduced at the start of granulation work, it is installed between the trough and the container and used for the purpose of sealing the container, and after the pressure inside the container has been reduced to zero, the slag flows into the trough 2: f
When the opening and closing plate is melted and the blast furnace slag starts to flow down into the depressurized container and is granulated, the depressurized state is maintained by the steam ejector 9.When the blast furnace slag flows down into the depressurized container 1, the molten slag is contained in the blast furnace slag. The N2, N2, and CO components in the slag become gases when exposed to low pressure and are released from the slag.

このガス放出過程において溶滓は細かく分散し、粒状化
されるのである。
During this gas release process, the slag is finely dispersed and granulated.

そして、この高炉滓膜8は減圧容器1内で脱ガス、冷却
され、容器底部に溜まると同時に、この部分に内蔵され
たスクリュウコンベヤー5により容器外へ搬出され、ベ
ルトコンベヤー6により搬送される。
Then, this blast furnace slag film 8 is degassed and cooled in the reduced pressure container 1 and collected at the bottom of the container, and at the same time is carried out of the container by a screw conveyor 5 built in this part and conveyed by a belt conveyor 6.

以下、この発明の実施例について説明する。Examples of the present invention will be described below.

実施例 1 第1表に示すガス成分を有する溶融高炉滓を1ton
、処理能力50kg/mmの前記減圧処理装置により減
圧容器内を10mπHgの真空度に保って処理した。
Example 1 1 ton of molten blast furnace slag having the gas components shown in Table 1
The treatment was carried out by maintaining the inside of the vacuum container at a vacuum level of 10 mπHg using the vacuum processing apparatus with a processing capacity of 50 kg/mm.

その結果、得られた高炉滓膜の性状を第2表に示す。As a result, the properties of the blast furnace slag film obtained are shown in Table 2.

この第2表から明らかなごとく、セメント原料の骨材と
して最適な粒径2〜511LNの高炉滓膜が大量に得ら
れ、しかも得られたいずれの粒径の高炉滓膜もすべて気
泡のない良質のものであった。
As is clear from Table 2, a large amount of blast furnace slag film with a particle size of 2 to 511 LN, which is optimal as an aggregate for cement raw materials, was obtained, and all of the obtained blast furnace slag films of any particle size were of good quality with no air bubbles. It belonged to

実施例 2 第1表に示すガス成分を有する溶融高炉滓を1ton、
処理能力50 kg/Inmの前記減圧処理装置により
減圧容器内を150mmHgの真空度に保ちトラフ内で
水蒸気をlog/iv溶融高炉滓に吹き込んで減圧処理
した。
Example 2 One ton of molten blast furnace slag having the gas components shown in Table 1,
The inside of the vacuum container was maintained at a vacuum level of 150 mmHg using the vacuum treatment apparatus having a processing capacity of 50 kg/Inm, and steam was blown into the log/iv melting blast furnace slag in the trough to perform the vacuum treatment.

その結果、得られた高炉滓膜の性状を第3表に示す。Table 3 shows the properties of the blast furnace slag film obtained as a result.

第3表から明らかなごとく、この場合も実施例1の場合
と同様に良質の高炉滓膜が大量に得られた。
As is clear from Table 3, a large amount of high quality blast furnace slag film was obtained in this case as well, as in Example 1.

以上説明したごとく、この発明法によれば、減圧容器を
使用するだけで、溶融高炉滓の粒状化処理が簡単かつ効
果的にできるうえ、強度的にもすぐれた高炉滓膜が得ら
れるので、溶融高炉滓の処理方法として極めて有効性、
実用性に富むものである。
As explained above, according to the method of the present invention, molten blast furnace slag can be easily and effectively granulated simply by using a vacuum vessel, and a blast furnace slag film with excellent strength can be obtained. Extremely effective as a treatment method for molten blast furnace slag,
It is highly practical.

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

第1図はこの発明法を実施するための減圧処理装置の一
例を示す縦断面図、第2図は減圧容器内圧力と平均粒径
の関係を示す図表である。 図中1・・・・・・減圧容器、2・・・・・・トラフ、
3・・・・・・開閉板、4・・・・・・シュート、5・
・・・・・搬出用スクリュウコンヘヤー、6・・・・・
・搬送用ベルトコンベヤー、7・・・・・・溶融高炉滓
、8・・・・・・高炉滓膜、9・・・・・・スチームエ
ジェクター。
FIG. 1 is a longitudinal sectional view showing an example of a reduced pressure treatment apparatus for carrying out the method of the present invention, and FIG. 2 is a chart showing the relationship between the internal pressure of the reduced pressure container and the average particle size. In the figure, 1...decompression vessel, 2...trough,
3...Opening/closing plate, 4...Chute, 5.
・・・・・・Screw container hair for carrying out, 6・・・・・・
- Belt conveyor for conveyance, 7... Molten blast furnace slag, 8... Blast furnace slag membrane, 9... Steam ejector.

Claims (1)

【特許請求の範囲】[Claims] 1 溶融高炉滓を造粒する方法において、気圧200m
mHg以下に減圧した減圧容器内に高炉溶滓を流下させ
前記溶滓を分散させて粒状化することを特徴とする溶融
高炉滓の造粒方法。
1 In a method of granulating molten blast furnace slag, an atmospheric pressure of 200 m
A method for granulating molten blast furnace slag, which comprises dispersing and granulating the molten slag by flowing the blast furnace slag into a vacuum vessel whose pressure is reduced to mHg or less.
JP9979676A 1976-08-20 1976-08-20 Granulation method of molten blast furnace slag Expired JPS5835943B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9979676A JPS5835943B2 (en) 1976-08-20 1976-08-20 Granulation method of molten blast furnace slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9979676A JPS5835943B2 (en) 1976-08-20 1976-08-20 Granulation method of molten blast furnace slag

Publications (2)

Publication Number Publication Date
JPS5325643A JPS5325643A (en) 1978-03-09
JPS5835943B2 true JPS5835943B2 (en) 1983-08-05

Family

ID=14256862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9979676A Expired JPS5835943B2 (en) 1976-08-20 1976-08-20 Granulation method of molten blast furnace slag

Country Status (1)

Country Link
JP (1) JPS5835943B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986004052A1 (en) * 1984-12-28 1986-07-17 Gosudarstvenny Sojuzny Institut Po Proektirovaniju Installation for granulation of metallurgic melt

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986004052A1 (en) * 1984-12-28 1986-07-17 Gosudarstvenny Sojuzny Institut Po Proektirovaniju Installation for granulation of metallurgic melt

Also Published As

Publication number Publication date
JPS5325643A (en) 1978-03-09

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