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JPH0621301B2 - Sintering method of iron ore - Google Patents
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JPH0621301B2 - Sintering method of iron ore - Google Patents

Sintering method of iron ore

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Publication number
JPH0621301B2
JPH0621301B2 JP25919185A JP25919185A JPH0621301B2 JP H0621301 B2 JPH0621301 B2 JP H0621301B2 JP 25919185 A JP25919185 A JP 25919185A JP 25919185 A JP25919185 A JP 25919185A JP H0621301 B2 JPH0621301 B2 JP H0621301B2
Authority
JP
Japan
Prior art keywords
iron ore
sintering
raw material
ore
blast furnace
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 - Lifetime
Application number
JP25919185A
Other languages
Japanese (ja)
Other versions
JPS62120434A (en
Inventor
教夫 栗原
富也 福田
俊雄 柳川
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 Nisshin Co Ltd
Original Assignee
Nisshin Steel 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 Nisshin Steel Co Ltd filed Critical Nisshin Steel Co Ltd
Priority to JP25919185A priority Critical patent/JPH0621301B2/en
Publication of JPS62120434A publication Critical patent/JPS62120434A/en
Publication of JPH0621301B2 publication Critical patent/JPH0621301B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,鉄鉱石の焼結法に関する。The present invention relates to a method for sintering iron ore.

〔従来の技術〕[Conventional technology]

高炉操業において,焼結鉱の性質特に被還元性(JIS-M87
13に規定の還元率)が良好であることが要求される。一
般に焼結鉱の低温還元粉化性が著しいと高炉シャフト部
の上部(300〜700℃付近)で還元されて粉化し,この粉化
程度が特に著しくなると炉内の通気性が損なわれてスリ
ップ,棚吊りなどを惹起させ炉内状況を不安定にする。
一方高炉に装入された焼結鉱は塊状で存在する間はCO+
2を主体とする炉内上昇ガスにより還元され,その後
溶融し,炉内を滴下する間に未還元部分は赤熱コークス
と直接的に反応して還元される。したがって溶融直前の
還元率が高いほどコークスの消費が少なくてすみ,高炉
の燃料比を低減させることができる。
In blast furnace operation, the properties of sinter are especially reducible (JIS-M87
The reduction rate specified in 13) is required to be good. Generally, if the low-temperature reductive pulverization property of sinter is remarkable, it will be reduced and pulverized at the upper part of the blast furnace shaft (around 300 to 700 ° C). , It causes hanging of the shelf and makes the inside of the furnace unstable.
On the other hand, the sintered ore charged into the blast furnace is CO +
It is reduced by the rising gas in the furnace mainly composed of N 2 , then melted, and the unreduced portion is directly reacted with the red hot coke and reduced while dropping inside the furnace. Therefore, the higher the reduction rate immediately before melting, the less the coke consumption, and the lower the fuel ratio in the blast furnace.

このようなことから,焼結鉱の被還元性を高めるため
に,焼結炉の製造にあたって,コークス粉等の燃料配合
率を適切に調節したうえ焼結温度を旧来の1350〜1450℃
から1200〜1300℃程度の比較的低い温度とし,これによ
って焼結鉱中のFeOを低くすることが提案され実施され
ている。より具体的には,焼結炉の微小気孔量を増加さ
せることと,ヘマタイトに比べて著しく被還元性の劣る
マグネタイトおよび非晶質けい酸塩中のFeO分を減少さ
せることが被還元性を高めるうえで有利となるので,燃
料配合率を適切に調節したうえでヘマタイトがマグネタ
イトと酸素に解難する温度より低い1200〜1300℃程度の
温度で焼結し,これによって微小気孔部が多く且つマグ
ネタイト生成量が少ない低FeOの被還元性の良好な焼結
鉱を製造する方法が実施されている。
Therefore, in order to increase the reducibility of the sinter, the sintering temperature should be adjusted from the conventional 1350 to 1450 ℃ while appropriately adjusting the blending ratio of fuel such as coke powder when manufacturing the sintering furnace.
Therefore, it has been proposed and implemented to lower the FeO content in the sinter by setting the temperature to a relatively low temperature of 1200 to 1300 ° C. More specifically, increasing the amount of micropores in the sintering furnace and reducing the FeO content in magnetite and amorphous silicate, which are significantly less reducible than hematite, reduce the reducibility. Since it is advantageous in increasing the temperature, it is necessary to adjust the fuel blending ratio appropriately and then sinter at a temperature of 1200 to 1300 ℃, which is lower than the temperature at which hematite is insoluble in magnetite and oxygen, which results in many micropores and magnetite. A method of producing a sinter having a low FeO content and a good reducibility is being implemented.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

焼結温度を低くして焼結する場合に,難溶融性鉄鉱石の
使用が制限されるという問題が起こる。鉄鉱石は銘柄に
よって成因や鉱物組織が異なり,焼結処理に供したとき
に1200〜1300℃の温度で同化し易いもの,し難いものが
ある。例えばオーストラリア産鉄鉱石は一般に上述の12
00〜1300℃の温度でかなり同化するのに対し,南アフリ
カ産鉄鉱石は一般には殆ど同化しない。
When sintering at a low sintering temperature, there is a problem that the use of refractory iron ore is limited. The origin and mineral structure of iron ore differ depending on the brand, and when subjected to sintering treatment, some are easy to assimilate at a temperature of 1200 to 1300 ° C, and some are difficult to assimilate. For example, Australian iron ore is generally
At a temperature of 00 to 1300 ℃, it is highly assimilated, whereas iron ore from South Africa is hardly assimilated.

資源ソースの分散等の理由により,一般には,種々の銘
柄の鉄鉱石を混合して焼結に供しているのが実情である
が,焼結過程で同化し難く天然鉱石のままの形態で焼結
鉱中に残存し易い傾向のある緻密質の難溶融性鉄鉱石を
配合した場合には,焼結温度を1200〜1300℃とすると,
被還元性の著しく劣る難溶融性鉄鉱石の鉱粒が焼結鉱中
にそのままの形で同化することなく多量に存在してしま
い,ヘマタイトの分解を防止すべく1200〜1300℃の温度
で焼結した場合に逆に焼結鉱の被還元性を劣化させるこ
とになる。したがって被還元性の良好な焼結鉱を得よう
とすると,かような難溶融性鉄鉱石の配合量を制限しな
ければならなくなる。
Due to the dispersion of resource sources, etc., in general, various brands of iron ore are mixed and used for sintering, but it is difficult to assimilate during the sintering process and burned in the form of natural ore. When a dense refractory iron ore, which tends to remain in the sinter, is added, if the sintering temperature is 1200 to 1300 ° C,
A large amount of refractory iron ore grains, which are extremely inferior in reducibility, were present in the sintered ore without being assimilated as they were, and were burned at a temperature of 1200 to 1300 ° C to prevent the decomposition of hematite. On the contrary, when it is bound, the reducibility of the sintered ore is deteriorated. Therefore, in order to obtain a sinter having good reducibility, it is necessary to limit the compounding amount of such refractory iron ore.

本発明は,かような問題点を解決すべく,難溶融性鉄鉱
石を配合しても良好な被還元性をもつ焼結鉱を従来と同
様の焼結条件で製造することを目的としてなされたもの
である。
In order to solve such a problem, the present invention has been made for the purpose of producing a sinter having a good reducibility even if a refractory iron ore is mixed under the same sintering conditions as the conventional one. It is a thing.

〔問題点を解決する手段〕[Means for solving problems]

本発明は,前記の目的を達成する処方として,複数の銘
柄からなる鉄鉱石を主原料とし,これに,返鉱,副原料
および固体燃料を混合して焼結原料を得るにさいし,難
溶融性鉄鉱石の銘柄を他の鉄鉱石の銘柄から選り分け, この選り分けた難溶融性鉄鉱石に,副原料の一部として
の石灰石または石灰石と生石灰,固体燃料の一部として
のコークス粉,および水砕高炉スラグを混合し,そのさ
い,この混合物中の水砕高炉スラグ含有率を2.5重量
%以下とし,そしてこの混合物に水を添加して造粒し, この造粒物を,残りの銘柄の鉄鉱石,返鉱,副原料およ
び固体燃料からなる混合物または造粒物に配合し造粒し
て焼結原料とし, この焼結原料を焼結機に供給して焼結することを特徴と
する。
According to the present invention, as a prescription for achieving the above-mentioned object, iron ore composed of a plurality of brands is used as a main raw material, and returning ore, an auxiliary raw material and a solid fuel are mixed to obtain a sintering raw material. The grade of refractory iron ore is selected from the brands of other iron ores, and the selected refractory iron ore is added to limestone or limestone and quick lime as a part of auxiliary materials, coke powder as a part of solid fuel, and water. When the ground blast furnace slag is mixed, the content of water granulated blast furnace slag in the mixture is adjusted to 2.5% by weight or less, and water is added to the mixture to granulate, and the granules are Characterized by blending into a mixture or granulation of brand iron ore, return ore, auxiliary raw material and solid fuel and granulating it as a sintering raw material, and supplying this sintering raw material to a sintering machine for sintering. And

ここで「難溶融性鉄鉱石」とは,前述したように,従来
法により1200〜1300℃の焼結温度で焼結したさいに焼結
過程で同化しがたく天然鉱石のままの形態で焼結鉱中に
残存する傾向のある緻密質の難溶融性の鉄鉱石を言う。
また本発明法は従来より広く使用されているドワイトロ
イド式焼結機を用いて焼結することを前提としている。
Here, "hardly soluble iron ore" means, as described above, a natural ore that is hard to assimilate during the sintering process when sintered by the conventional method at a sintering temperature of 1200 to 1300 ° C. It is a dense, infusible iron ore that tends to remain in the ore.
Further, the method of the present invention is premised on sintering using a Dwightroid type sintering machine which has been widely used.

本発明者らは前記目的において種々の試験研究を重ねた
が,製鉄所内で製造している水砕高炉スラグがその使用
の仕方によってこの目的達成に好適に利用できることが
わかった。水砕高炉スラグの組成の一例を第1表に示し
たが,この例に見られるように,水砕高炉スラグはかな
りの量のCaOおよびAl2O3を含有している。
The inventors of the present invention have conducted various tests and researches for the above purpose, and found that the granulated blast furnace slag produced in the steel mill can be suitably used for achieving this purpose depending on the way of use. An example of the composition of the granulated blast furnace slag is shown in Table 1. As seen in this example, the granulated blast furnace slag contains a considerable amount of CaO and Al 2 O 3 .

本発明法では,このような水砕高炉スラグを焼結原料へ
の添加剤として使用するのであるが,そのさい,先ず,
選り分けた難溶融性鉄鉱石に対して,この水砕高炉スラ
グを,副原料の一部としての石灰石または石灰石と生石
灰,固体燃料の一部としてのコークス粉と共に配合し,
回転ドラムなどの設備を用いて混合並びに造粒する。こ
の場合の水砕炉スラグの添加量は,難溶融生鉄鉱石,石
灰石または石灰石と生石灰,コークス粉および水砕高炉
スラグからなる混合物100重量部に対して2.5重量部
までとする。つまり,この混合物の2.5重量%までと
するのがよい。これ以上の添加量でも焼結鉱の還元率は
向上するが,あまり多いと成品焼結鉱中のスラグ量を増
加させることになり,この焼結鉱を高炉に装入した場合
にコークス比が増加することになる。後記実施例に示す
ように2.5重量%までの水砕高炉スラグの配合量によ
り十分の還元率向上効果が得られる。なお水砕高炉スラ
グの添加にさいしては,出来るだけ粉状のものを使用す
るのがよく,好ましくは平均粒子径が0.5mm以下のも
のを使用するのがよい。
In the method of the present invention, such granulated blast furnace slag is used as an additive to the sintering raw material.
The granulated blast furnace slag is mixed with the selected refractory iron ore together with limestone or limestone and quicklime as a part of auxiliary materials, and coke powder as a part of solid fuel,
Mix and granulate using equipment such as a rotating drum. In this case, the addition amount of the granulating furnace slag is up to 2.5 parts by weight with respect to 100 parts by weight of the refractory raw iron ore, limestone or a mixture of limestone and quicklime, coke powder and granulated blast furnace slag. That is, up to 2.5% by weight of this mixture is recommended. If the amount added exceeds this value, the reduction rate of the sinter will improve, but if it is too large, the amount of slag in the product sinter will increase, and when the sinter is charged into the blast furnace, the coke ratio will increase. Will increase. As shown in Examples below, a sufficient reduction rate improvement effect can be obtained by blending the amount of granulated blast furnace slag up to 2.5% by weight. When adding the granulated blast furnace slag, it is preferable to use powdery one as much as possible, preferably one having an average particle diameter of 0.5 mm or less.

このようにして,難溶融成鉄鉱石,石灰石または石灰石
と生石灰,コークス粉および水砕高炉スラグを適切な配
合量のもとで混合し,この混合物に水を加えて造粒する
のであるが,本発明法においては,この造粒物を,残り
の銘柄の鉄鉱石の原料配合物(鉄鉱石,返鉱,副原料お
よび固体燃料からなる混合物または造粒物)に配合し,
全体を造粒して焼結原料とする。この関係を第1図に示
した。
In this way, refractory iron ore, limestone or limestone and quicklime, coke powder and granulated blast furnace slag are mixed in an appropriate amount, and water is added to this mixture for granulation. In the method of the present invention, the granulated product is blended with the raw material mixture of the remaining brand of iron ore (a mixture or granulated product of iron ore, return ore, auxiliary raw material and solid fuel),
The whole is granulated and used as a sintering raw material. This relationship is shown in FIG.

第1図における右側のA系統は,粉状鉄鉱石,返鉱,副
原料および固体燃料からなる焼結原料から焼結鉱を得る
基本フローを示しているが,本発明においては,この焼
結原料中の粉状鉄鋼石のうち緻密質の難溶融性鉄鉱石を
選り分けて左側のB系統に使用する。このB系統に使用
する石灰石または石灰石と生石灰並びに固体燃料として
は,A系統の副原料の一部および固体燃料の一部をこの
B系統にまわすことができる。B系統においては前述の
ように,難溶融性鉄鉱石,石灰石または石灰石と生石
灰,コークス粉および水砕高炉スラグを,これらの配合
物中の水砕高炉スラグ含有率が2.5重量%以下となる
ように配合し,回転ドラム等の設備により混合しまた水
を加えて造粒する。このB系統で製造した造粒物を,A
系統の4種の出発原料である粉状鉄鉱石,返鉱,副原料
および固体燃料と共に混合するか,またはこの4種の出
発原料を混合したものに混合し造粒して焼結機に装填す
る。ここで,A系統の副原料とは蛇紋岩,珪砂,石灰石
などを指す。固体燃料は通常はコークス粉である。
The system A on the right side in FIG. 1 shows a basic flow for obtaining a sintered ore from a sintering raw material composed of powdered iron ore, returning ore, an auxiliary raw material, and a solid fuel. In the present invention, this sintering is performed. Of the powdered iron ore in the raw material, the dense refractory iron ore is selected and used for the B line on the left side. As the limestone or limestone and quick lime and the solid fuel used in the B system, a part of the auxiliary raw material of the A system and a part of the solid fuel can be passed to the B system. In the B system, as described above, refractory iron ore, limestone or limestone and quick lime, coke powder and granulated blast furnace slag, and the content ratio of granulated blast furnace slag in these compounds is 2.5% by weight or less. Mix as follows, mix with equipment such as a rotating drum, and add water to granulate. Granules produced by this B system are
Mix with 4 kinds of starting materials of powdered iron ore, return ore, auxiliary materials and solid fuel, or mix with 4 kinds of starting materials, granulate and load into sintering machine To do. Here, the auxiliary raw materials of system A refer to serpentine, silica sand, limestone, and the like. The solid fuel is usually coke flour.

このような処法により,難溶融性鉄鉱石を配合した焼結
原料でも1200〜1300℃での低温焼結において被還元性の
良好な焼結鉱を高い生産率のもとで製造することができ
る。その理由としては,難溶融性鉄鉱石だけを選り分け
てこれに水砕高炉スラグ,石灰石または石灰石と生石灰
およびコークス粉が混合造粒してから,この造粒物を全
焼結原料中に配合するので,全焼結原料中における難溶
融性鉄鉱石の各粒子の近傍には水砕高炉スラグ,石灰石
または石灰石と生石灰およびコークス粉が濃縮して存在
することになり,この状態で焼結を行うと難溶融性鉄鉱
石の各粒子の周囲に低融点融液が生成し易くなり,この
低融点融液に難溶融性鉄鉱石が同化するようになるから
であると考えられる。また,水砕高炉スラグは第1表に
示されるようにかなりのAl2O3とCaOを含有しているが,
難溶融性鉄鉱石中のFe2Oと石灰石や生石灰中或いは水
砕高炉スラグ中のCaOとが反応して生成したCaO-Fe2O3
融液へのAl2O3の溶け込み量が増大することによりカル
シウムフェライト生成量を増大させることができるので
あろうと考えられる。このようなことから,従来におい
て1200〜1300℃で焼結する方法ではほとんど同化するこ
となしに天然鉱石のままの形で焼結鉱中に残存するよう
な被還元性の著しく劣る難溶融性鉄鉱石でも,本発明法
によると,カルシウムフェライトおよび微細なヘマタイ
トに変化させることができることになり,その結果,被
還元性の良好な焼結鉱を得ることができる。
By such a method, it is possible to produce a sintered ore with good reducibility at a high production rate even at a sintering raw material containing a refractory iron ore at low temperatures of 1200 to 1300 ℃. it can. The reason for this is that only the refractory iron ore is selected and granulated blast furnace slag, limestone or limestone and quick lime and coke powder are mixed and granulated, and then this granulated material is mixed in all the sintering raw materials. , Granulated blast-furnace slag, limestone or limestone and quicklime and coke powder exist in the vicinity of each particle of refractory iron ore in the whole sintering raw material, and it is difficult to sinter in this state. It is considered that this is because a low melting point melt is likely to be formed around each particle of the melting point iron ore, and the refractory iron ore is assimilated into the low melting point melt. Also, as shown in Table 1, granulated blast furnace slag contains a considerable amount of Al 2 O 3 and CaO,
The amount of Al 2 O 3 dissolved in the CaO-Fe 2 O 3 -based melt formed by the reaction of Fe 2 O 3 in refractory iron ore with CaO in limestone, quick lime or granulated blast furnace slag It is considered that the amount of calcium ferrite produced can be increased by increasing the amount. Therefore, in the conventional method of sintering at 1200 to 1300 ° C, refractory iron ore with remarkably inferior reducibility that remains in the sinter in the form of natural ore with almost no assimilation Even with stones, according to the method of the present invention, calcium ferrite and fine hematite can be converted, and as a result, a sintered ore with good reducibility can be obtained.

本発明の実施にさいし,使用する水砕高炉スラグの代わ
りに,高炉スラグを徐冷して高炉バラス製造する時の整
流過程で発生する粉部分を使用してもよいが,この場合
には,Sを1.0重量%程度含有しているので使用に際
して量の制限が必要となる。
In practicing the present invention, instead of the granulated blast furnace slag used, a powder portion generated in the rectification process at the time of slowly cooling the blast furnace slag to produce the blast furnace ballast may be used, but in this case, Since S is contained in an amount of about 1.0% by weight, it is necessary to limit the amount in use.

〔実施例〕〔Example〕

実施例1 第2表に本例の焼結原料の配合割合を示した。第2表中
の従来法(A0)は,第1図におけるA系統だけに相当
するものであり,この場合には,粉状鉄鉱石原料に緻密
質の難溶融性鉄鉱石もそのまま配合したものである。第
2表中のBは,第1図のように,粉状鉄鉱石のうちから
難溶融性鉄鋼石を選り分け,これにA系統中の石灰石,
生石灰およびコークス粉の一部をとり,更に平均粒子径
が0.5mm以下の水砕高炉スラグを配合したものであ
る。この配合物Bは回転ドラムで水を加えて造粒したあ
と,第1図のフローに示すように,第二ミキサーで他の
原料を混合したものと混合した。第2表中における水砕
高炉スラグの配合量は,全焼結原料に対する量で示して
あるが,B配合中の量に換算すると,B配合100重量部
に対し1.5重量部となる。従来法および本発明法とも
焼結原料を同じ焼結機に装填し,両者とも同じ焼結条件
のもとで焼結した。
Example 1 Table 2 shows the mixing ratio of the sintering raw material of this example. The conventional method (A 0 ) in Table 2 corresponds only to the A system in FIG. 1, and in this case, the powdery iron ore raw material was also blended with the dense refractory iron ore as it was. It is a thing. As shown in Fig. 1, B in Table 2 selects refractory iron ore from the powdered iron ore, and limestone in system A,
It is a mixture of granulated blast furnace slag with an average particle size of 0.5 mm or less, in which a portion of quicklime and coke powder is taken. This compound B was granulated by adding water with a rotary drum and then mixed with another raw material by a second mixer as shown in the flow chart of FIG. The blending amount of the granulated blast furnace slag in Table 2 is shown as the amount relative to all the sintering raw materials, but when converted to the amount in the B blending, it becomes 1.5 parts by weight based on 100 parts by weight of the B blending. In the conventional method and the method of the present invention, the sintering raw materials were loaded into the same sintering machine, and both were sintered under the same sintering conditions.

得られた焼結炉をJIS-M8713に準拠した試験に供しその
還元率を調べた。その結果を第3表に示した。また生産
率も第3表に併せて示した。
The obtained sintering furnace was subjected to a test in accordance with JIS-M8713 and its reduction rate was investigated. The results are shown in Table 3. The production rate is also shown in Table 3.

第3表の結果より,本発明法によると従来法に比べて同
じ生産率のもとで還元率が0.6%上昇した焼結鉱が得
られたことがわかる。
From the results in Table 3, it can be seen that according to the method of the present invention, a sinter having a reduction rate increased by 0.6% was obtained under the same production rate as in the conventional method.

実施例2 易溶融性のオーストラリア産の鉄鉱石の配合割合を減少
し,難溶融性の南アフリカ産の鉄鉱石の配合割合を増加
させたこと以外は,実施例1と同じようにして3種類の
焼結原料を作り,これらを同じ焼結条件のもとで焼結し
た。その配合割合を実施例1と同様の基準で第4表に示
した。
Example 2 Three kinds of materials were prepared in the same manner as in Example 1 except that the blending ratio of the easily meltable Australian iron ore was decreased and the blending ratio of the refractory South African iron ore was increased. We made sintering raw materials and sinter them under the same sintering conditions. The blending ratio is shown in Table 4 on the same basis as in Example 1.

各々の焼結品の生産率と還元性を第5表に示した。Table 5 shows the production rate and reducibility of each sintered product.

第5表の結果から,本発明法によると,難溶融性鉄鉱石
の配合割合を約18%と多くした場合でも生産率を低下さ
せることなく還元率を上昇できたことがわかる。
From the results in Table 5, it can be seen that according to the method of the present invention, the reduction rate could be increased without lowering the production rate even when the blending ratio of the refractory iron ore was increased to about 18%.

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

第1図は本発明法の製造工程を説明するための工程図で
ある。
FIG. 1 is a process drawing for explaining the manufacturing process of the method of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】複数の銘柄からなる鉄鉱石を主原料とし,
これに,返鉱,副原料および固体燃料を混合して焼結原
料を得るにさいし, 難溶融性鉄鉱石の銘柄を他の鉄鉱石の銘柄から選り分
け, この選り分けた難溶融性鉄鉱石に,前記の副原料の一部
としての石灰石または石灰石と生石灰,固体燃料の一部
としてのコークス粉,および水砕高炉スラグを混合して
混合物中の水砕高炉スラグ含有率を2.5重量%以下と
し,そしてこれに水を添加して造粒し, この造粒物を,残りの銘柄の鉄鉱石,返鉱,副原料およ
び固体燃料からなる混合物または造粒物に配合し造粒し
て焼結原料とし, この焼結原料を焼結機に供給して焼結することからなる
鉄鉱石の焼結法。
1. A main raw material is iron ore composed of a plurality of brands,
In this, when returning ore, auxiliary raw material and solid fuel are mixed to obtain a sintering raw material, the brands of refractory iron ore are selected from the brands of other iron ores, and the selected refractory iron ores are The content of granulated blast furnace slag in the mixture is not more than 2.5 wt% by mixing limestone or limestone and quicklime as a part of the above-mentioned auxiliary materials, coke powder as a part of solid fuel, and granulated blast furnace slag. Then, water is added to this to granulate, and this granulated product is blended with a mixture or granulated product of the remaining brand of iron ore, return ore, auxiliary raw material and solid fuel and granulated and fired. Sintering method of iron ore, which is used as a binding raw material, and this sintering raw material is supplied to a sintering machine and sintered.
JP25919185A 1985-11-19 1985-11-19 Sintering method of iron ore Expired - Lifetime JPH0621301B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25919185A JPH0621301B2 (en) 1985-11-19 1985-11-19 Sintering method of iron ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25919185A JPH0621301B2 (en) 1985-11-19 1985-11-19 Sintering method of iron ore

Publications (2)

Publication Number Publication Date
JPS62120434A JPS62120434A (en) 1987-06-01
JPH0621301B2 true JPH0621301B2 (en) 1994-03-23

Family

ID=17330635

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25919185A Expired - Lifetime JPH0621301B2 (en) 1985-11-19 1985-11-19 Sintering method of iron ore

Country Status (1)

Country Link
JP (1) JPH0621301B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9409360B2 (en) 2007-11-15 2016-08-09 Pirelli Tyre S.P.A. Process for manufacturing tyres for vehicle wheels and apparatus for building a carcass structure of a tyre for vehicle wheels

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112961978B (en) * 2021-02-01 2023-03-17 山西太钢不锈钢股份有限公司 Method for reducing powder rate in pellet production process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9409360B2 (en) 2007-11-15 2016-08-09 Pirelli Tyre S.P.A. Process for manufacturing tyres for vehicle wheels and apparatus for building a carcass structure of a tyre for vehicle wheels

Also Published As

Publication number Publication date
JPS62120434A (en) 1987-06-01

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