JPH07331344A - Method for controlling permeable gas in exhaust gas circulated sintering - Google Patents

Method for controlling permeable gas in exhaust gas circulated sintering

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Publication number
JPH07331344A
JPH07331344A JP14558994A JP14558994A JPH07331344A JP H07331344 A JPH07331344 A JP H07331344A JP 14558994 A JP14558994 A JP 14558994A JP 14558994 A JP14558994 A JP 14558994A JP H07331344 A JPH07331344 A JP H07331344A
Authority
JP
Japan
Prior art keywords
sintering
raw material
exhaust gas
ore
difficult
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.)
Withdrawn
Application number
JP14558994A
Other languages
Japanese (ja)
Inventor
Yoshiaki Shimakawa
義明 島川
Junichiro Ikenaga
淳一郎 池永
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
Nippon Steel Corp
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 Steel Corp filed Critical Nippon Steel Corp
Priority to JP14558994A priority Critical patent/JPH07331344A/en
Publication of JPH07331344A publication Critical patent/JPH07331344A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To improve the gas permeability in a sintering layer and to improve the yield and the productivity of sintered ore by blending difficult-to-melting ore in sintering raw material in an exhaust gas-circulated permeable gas control. CONSTITUTION:In the permeable gas control method in the exhaust gas circulated sintering, by which the exhaust gas exhausted from a sintering machine is again returned back to a sintering bed to reuse this exhaust gas as the heat source for sintering the sintering raw material, the difficult-to-melting ore, such as qualtz series ore, etc., is blended at 20-50% in the sintering raw material. In the combustion part in the ordinary main raw material grain, the surface of the main raw material grain is melted by the combustion heat and becomes the condition of combining the adjacent main raw material grains and the permeability around these grains is lowered. Therefore, as the blended difficult- to-melted ore is difficult to melt by the combustion heat, the combination between the grains is cut off at the part of the difficult-to-melted ore and the gas permeability of the sintering layer is improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、排ガス循環焼結通気制
御方法に係り、更に詳しくは、焼結層の通気性を向上さ
せて、下層赤熱帯の厚さを減少させることにより、焼結
鉱の歩留りや生産性を向上できる排ガス循環焼結通気制
御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas circulation sintering aeration control method, and more particularly to a method for improving the air permeability of a sintered layer to reduce the thickness of the lower red tropical zone. The present invention relates to an exhaust gas circulation sintering aeration control method capable of improving the yield and productivity of ore.

【0002】[0002]

【従来の技術】例えば、特開昭54−104403号公
報の「焼結鉱の製造法」に記載されているように、一般
的な連続焼結機であるドワイトロイド式の焼結機におい
ては、焼結原料と共に焼結ベッド上に装入されるコーク
スとして、粒度0.5〜3mmのものが使用されてい
る。その平均粒度は、特開昭54−129003号公報
の「小球状コークスの製造方法」や、特開昭53−37
103号公報の「NOx抑制焼結操業法」に記載されて
いるように、通常1〜2mmである。また、他の連続焼
結方法として、焼結機から排出される排ガスを、再度、
焼結ベッドに戻して再使用する排ガス循環焼結方法が知
られている。
2. Description of the Related Art For example, as described in Japanese Unexamined Patent Publication (Kokai) No. 54-104403, "Manufacturing Method of Sintered Ore", in a Dwightroid type sintering machine which is a general continuous sintering machine, The coke charged with the sintering raw material on the sintering bed has a grain size of 0.5 to 3 mm. The average particle size is described in JP-A No. 54-129003, “Method for producing small spherical coke” and JP-A No. 53-37.
It is usually 1 to 2 mm as described in "NOx Suppressing Sintering Method" in Japanese Patent Laid-Open No. 103. Further, as another continuous sintering method, the exhaust gas discharged from the sintering machine is again
An exhaust gas circulation sintering method of returning to a sintering bed for reuse is known.

【0003】[0003]

【発明が解決しようとする課題】この排ガス循環焼結方
法では、100〜300度の高温の排ガスを焼結ベッド
に戻すので、焼結ベッド上の層内の通気抵抗は大きく、
通過風量が減少してしまう。また、排ガスが高温である
ので、焼結ベッド上の焼結層の冷却が遅くなり、110
0度以上の溶融部であって、圧損が他の原料層や焼結層
の約2倍(図4のグラフ参照)もある赤熱帯、特に下層
赤熱帯の厚さが増加し、これにより原料燃焼時における
焼結ベッド上の層全体の通気性が低下して、歩留りや生
産性が低下するという問題点があった。
In this exhaust gas circulation sintering method, since the exhaust gas at a high temperature of 100 to 300 degrees is returned to the sintering bed, the ventilation resistance in the layer on the sintering bed is large,
The amount of passing air will decrease. In addition, since the exhaust gas is at a high temperature, the cooling of the sintered layer on the sintering bed is delayed,
The thickness of the red tropics, especially in the lower red tropics, which is a fusion zone of 0 degrees or more and whose pressure loss is about twice that of other raw material layers and sintered layers (see the graph in Fig. 4), increases the raw material. There is a problem in that the air permeability of the entire layer on the sintering bed during combustion is reduced, and the yield and productivity are reduced.

【0004】実際に、前記平均粒度1〜2mmの粉状コ
ークスにより焼結作業を行ってみると、1個の粉状コー
クスが完全燃焼するまでに6〜7分の時間がかかり、燃
焼後期の下層赤熱帯の厚さは、ドワイトロイド式では平
均100mmであったのに対してほぼ150mmと増加
し、これにより焼結ベッド上の層全体の通気性が低下す
る。従って、焼結ベッドの送り速度が一定であれば、焼
結鉱が不完全焼成のまま排出されて歩留りが悪くなり、
また一定基準の歩留りを確保するために焼結ベッドの送
り速度を遅くすれば、生産性が低下することになる。そ
こで、本発明者は、従来、燃焼原料中に10%程度しか
配合されていなかったリオドセ(商品名)などの難溶融
鉱石に着目し、この難溶融鉱石の配合量を増やすことに
より、焼結層の通気度を調整する方法を開発するに到っ
た。
Actually, when the sintering work is performed using the powdery coke having the average particle size of 1 to 2 mm, it takes 6 to 7 minutes until one powdery coke completely burns, and it takes about 6 to 7 minutes in the latter stage of combustion. The thickness of the lower red tropics increased to almost 150 mm, compared to an average of 100 mm in the Dwightroid equation, which reduces the air permeability of the entire layer on the sintering bed. Therefore, if the feed rate of the sintering bed is constant, the sintered ore will be discharged incompletely fired and the yield will deteriorate,
Further, if the feed rate of the sintering bed is slowed down to secure the yield of a certain standard, the productivity will decrease. Therefore, the present inventor has focused on difficult-to-melt ores such as Riodoce (trade name), which has been conventionally mixed in the combustion raw material in an amount of only about 10%, and increases the amount of the hard-to-melt ores to perform sintering. It came to develop a method of adjusting the air permeability of a layer.

【0005】本発明はかかる事情に鑑みてなされたもの
で、焼結層の通気性を向上させて、焼結鉱の歩留りや生
産性を向上できる排ガス循環焼結通気制御方法を提供す
ることを目的とする。
The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide an exhaust gas circulation sintering aeration control method capable of improving the air permeability of a sintered layer to improve the yield and productivity of the sintered ore. To aim.

【0006】[0006]

【課題を解決するための手段】前記目的に沿う請求項1
記載の排ガス循環焼結通気制御方法は、焼結機から排出
される排ガスを、再度、焼結ベッドに戻して焼結原料を
焼結する熱源として再使用する排ガス循環焼結の通気制
御方法において、焼結原料中に、難溶融鉱石を20〜5
0%配合させるように構成されている。なお、ここでい
う難溶融鉱石とは、例えばリオドセ、MBR、ヤンピー
(以上、商品名)といった石英系鉱石をいう。また、石
英系鉱石としてはSiO2 が0.3〜5.5%、Al2
3 が2%以下であり、結晶水を2%以下含有してお
り、緻密質で難溶融性である。
A method according to the above-mentioned object.
Exhaust gas circulation sintering ventilation control method described, the exhaust gas discharged from the sintering machine, again, in the ventilation control method of exhaust gas circulation sintering to return to the sintering bed and reuse as a heat source for sintering the sintering raw material , 20 to 5 refractory ore in the sintering raw material
It is configured to be blended with 0%. The refractory ore referred to here is, for example, quartz-based ore such as Riodose, MBR, and Yampy (above, trade name). Further, as the quartz-based ore, SiO 2 is 0.3 to 5.5%, Al 2
O 3 is 2% or less, water of crystallization is 2% or less, and it is dense and hardly melts.

【0007】[0007]

【作用】請求項1記載の排ガス循環焼結通気制御方法に
おいては、焼結原料中に、難溶融鉱石を20〜50%配
合させて焼結を行うと、通常の主原料粒の燃焼部分で
は、燃焼熱により主原料粒の表面が溶融して、隣接する
主原料粒どうしが結合した状態になり、その周辺の通気
性は低下するが、配合される難溶融鉱石は燃焼熱により
溶け難いので、この難溶融鉱石の部分で粒どうしの結合
が断ち切られ、焼結層の通気性が向上し、焼結鉱の歩留
りや生産性が向上する。
In the exhaust gas circulation sintering aeration control method according to the first aspect, when 20 to 50% of the refractory ore is mixed in the sintering raw material and the sintering is performed, in the burning portion of the usual main raw material grains. , The surface of the main raw material grains is melted by the heat of combustion, and the adjacent main raw material grains are bonded to each other, and the air permeability in the periphery is reduced, but the refractory ore to be blended is difficult to melt due to the combustion heat. The grain-to-grain bonds are cut off at the portion of the difficult-to-melt ore, the air permeability of the sintered layer is improved, and the yield or productivity of the sintered ore is improved.

【0008】[0008]

【実施例】続いて、添付した図面を参照しつつ、本発明
を具体化した実施例につき、説明し、本発明の理解に供
する。ここに、図1は本発明の一実施例に係る排ガス循
環焼結通気制御方法による焼結進行状況を示す説明図、
図2はリオドセ配合量に対する下層赤熱帯の厚さの関係
を示すグラフ、図3はリオドセ配合量に対する焼結時間
と成品歩留りとの関係を示すグラフである。
Embodiments of the present invention will now be described with reference to the accompanying drawings to provide an understanding of the present invention. Here, FIG. 1 is an explanatory view showing the progress of sintering by an exhaust gas circulation sintering aeration control method according to an embodiment of the present invention,
FIG. 2 is a graph showing the relationship between the amount of Riodoce mixed with the thickness of the lower red tropical zone, and FIG. 3 is a graph showing the relationship between sintering time and product yield with respect to the compounded amount of Riodoce.

【0009】本発明の一実施例に係る排ガス循環焼結通
気制御方法は、焼結機からメインダクトを介して排出さ
れる排ガスを、ブロアにより焼結ベッドに戻して再使用
する排ガス循環焼結の通気制御方法である。焼結ベッド
上には、コークスが配合された焼結原料が装入ホッパよ
り装入され、焼結機の点火炉において原料層の上部に点
火され、保熱炉を通過中に高温の赤熱帯が徐々に下層に
下り(図1参照)、焼結機から排出されるまでに燃焼が
終了する。その後、生産された焼結鉱は、1次クラッシ
ャにより破砕され、クーラ中で冷却される。
The exhaust gas circulation sintering ventilation control method according to an embodiment of the present invention is an exhaust gas circulation sintering method in which exhaust gas discharged from a sintering machine through a main duct is returned to a sintering bed by a blower and reused. This is a ventilation control method. On the sintering bed, the sintering raw material mixed with coke is charged from the charging hopper and ignited at the upper part of the raw material layer in the ignition furnace of the sintering machine. Gradually descends to the lower layer (see FIG. 1), and the combustion ends by the time it is discharged from the sintering machine. After that, the produced sinter is crushed by the primary crusher and cooled in the cooler.

【0010】さて、本発明の排ガス循環焼結通気制御方
法の特徴は、焼結原料中に難溶融鉱石を配合させること
により焼結層の通気性を向上させ、これにより成品であ
る焼結鉱の歩留りや生産性を向上させた点にある。難溶
融鉱石としては、例えばリオドセ、MBR、ヤンピーな
どの溶融温度1250〜1330度の石英系鉱石が使用
できる。難溶融鉱石を焼結原料中に配合させる割合は、
20〜50%、特に30〜45%が好ましい。難溶融鉱
石の配合割合が20%未満では、焼結層の通気性が悪く
なって下層赤熱帯が厚くなり(図2参照)、これにより
焼結時間が長くなり生産性が低下してしまう。また、5
0%を超えると焼結時間は変わらないものの、焼結鉱中
に含まれて欲しくない難溶融鉱石の割合が増加するの
で、成品歩留りは低下する(図3参照)。
The characteristic feature of the exhaust gas circulation sintering aeration control method of the present invention is that the gas permeability of the sintered layer is improved by adding a refractory ore to the sintering raw material, and as a result, a sintered ore product is obtained. It is the point that the yield and productivity have been improved. As the refractory ore, it is possible to use, for example, quartz-based ores with a melting temperature of 1250 to 1330 degrees, such as Riodose, MBR, and Yampy. The ratio of the refractory ore mixed in the sintering raw material is
20 to 50%, especially 30 to 45% is preferable. If the blending ratio of the refractory ore is less than 20%, the air permeability of the sintered layer becomes poor and the lower red tropical zone becomes thicker (see FIG. 2), which results in longer sintering time and lower productivity. Also, 5
If it exceeds 0%, the sintering time does not change, but the ratio of the refractory ore that is not desired to be contained in the sintered ore increases, so the product yield decreases (see FIG. 3).

【0011】図3のグラフに示すように、難溶融鉱石を
焼結原料中に20〜50%配合させると、燃焼時におい
て、83〜84%くらいの高い成品歩留りを維持して、
焼結時間を35〜36分間くらいまで短縮でき、これに
より図2に示すように、下層赤熱帯の厚さが、従来15
0mm(リオドセ配合量10%)であったのが、100
mm程度まで薄くなる。
As shown in the graph of FIG. 3, when the refractory ore is mixed in the sintering raw material in an amount of 20 to 50%, a high product yield of about 83 to 84% is maintained during combustion.
The sintering time can be shortened to about 35 to 36 minutes, and as a result, as shown in FIG.
0 mm (10% of the amount of riodose) was 100
It becomes thin to about mm.

【0012】焼結原料の主原料粒は、1100度の高温
の赤熱帯において、その燃焼熱により粒表面が溶融し、
隣接する主原料粒どうしが結合した状態になる。従っ
て、粒間の隙間は塞がれて、周辺の通気性が低下する。
一方、難溶融鉱石は燃焼熱により溶け難いので、この難
溶融鉱石の部分で粒どうしの結合が断ち切られ、この部
分で焼結層の通気性が向上する。これにより、下層赤熱
帯は薄くなり、原料層の焼結時間が短縮され、従来では
下層赤熱帯が厚いために、焼結鉱が不完全焼成のまま排
出されて歩留りが悪くなっていたのが、本発明では所定
の焼結ベッドの送り時間中に、焼結原料が完全焼成され
るので歩留りが向上する。また、従来では、このように
焼結鉱が不完全焼成のまま排出される虞れが大きいの
で、焼結ベッドの送り速度を高速化し難かったが、本発
明では原料層の燃焼速度が速くなるので、焼結ベッドの
送り速度を高速化しても十分に対応でき、これにより焼
結鉱の生産性が向上できる。
The main raw material grains of the sintering raw material are melted on the surface of the grains due to the combustion heat in the red tropical zone at a high temperature of 1100 degrees
The adjacent main raw material grains are bonded together. Therefore, the gaps between the grains are closed, and the air permeability in the periphery is reduced.
On the other hand, since the refractory ore is difficult to melt due to combustion heat, the bonds between the grains are cut off at the refractory ore portion, and the air permeability of the sintered layer is improved at this portion. As a result, the lower red tropical zone becomes thin, the sintering time of the raw material layer is shortened, and in the past, since the lower red tropical zone was thick, the sintered ore was discharged as incompletely fired, resulting in poor yield. In the present invention, since the sintering raw material is completely fired during the predetermined feeding time of the sintering bed, the yield is improved. Further, in the past, since there is a high possibility that the sintered ore will be discharged as it is incompletely fired, it was difficult to increase the feed rate of the sintering bed, but in the present invention, the burning rate of the raw material layer is increased. Therefore, even if the feeding speed of the sintering bed is increased, it is possible to sufficiently cope with it, and thus the productivity of the sintered ore can be improved.

【0013】以下、表1を参照しながら、本発明の排ガ
ス循環焼結通気制御方法による焼結例と、従来の排ガス
循環焼結通気制御方法による焼結例とを具体的に比較し
て説明する。
Hereinafter, referring to Table 1, a specific comparison will be made between a sintering example by the exhaust gas circulation sintering and ventilation control method of the present invention and a sintering example by the conventional exhaust gas circulation sintering and ventilation control method. To do.

【0014】[0014]

【表1】 [Table 1]

【0015】表1から明らかなように、焼結原料中に難
溶融鉱石を20%または45%配合させると、下層赤熱
帯の厚さは従来法のもののほぼ3分の2まで薄くなり、
従来法による生産性は31.0T/D・m2 であったの
が、実施例1では34T/D・m2 、実施例2では35
T/D・m2 とほぼ10%向上し、また成品歩留りも、
従来法では84.0%であったのが、実施例1では8
4.5%、実施例2では84.3%と向上した。
As is clear from Table 1, when 20% or 45% of refractory ore is mixed in the sintering raw material, the thickness of the lower red tropical zone is reduced to almost two-thirds that of the conventional method.
The productivity by the conventional method was 31.0T / D · m 2 is Example 1, 34T / D · m 2, in Example 2 35
Approximately 10% improvement in T / D · m 2 and product yield
It was 84.0% in the conventional method, but was 8 in Example 1.
It was improved to 4.5% and to 84.3% in Example 2.

【0016】[0016]

【発明の効果】請求項1記載の排ガス循環焼結通気制御
方法は、このように焼結原料中に難溶融鉱石を20〜5
0%配合させるようにしたので、焼結層の通気性が向上
し、これにより下層赤熱帯の厚さが薄くなり、焼結時間
が短縮されて、焼結鉱の歩留りや生産性が向上できる。
According to the exhaust gas circulation sintering ventilation control method of the first aspect of the present invention, 20 to 5 refractory ores are contained in the sintering raw material.
Since the content of 0% is mixed, the air permeability of the sintered layer is improved, which reduces the thickness of the lower red tropical zone, shortens the sintering time, and improves the yield and productivity of the sintered ore. .

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

【図1】本発明の一実施例に係る排ガス循環焼結通気制
御方法による焼結進行状況を示す説明図である。
FIG. 1 is an explanatory diagram showing the progress of sintering by an exhaust gas circulation sintering aeration control method according to an embodiment of the present invention.

【図2】リオドセ配合量に対する下層赤熱帯の厚さの関
係を示すグラフである。
FIG. 2 is a graph showing the relationship between the amount of Riodoce and the thickness of the lower red tropical zone.

【図3】リオドセ配合量に対する焼結時間と成品歩留り
との関係を示すグラフである。
FIG. 3 is a graph showing the relationship between the sintering time and the product yield with respect to the blending amount of riodose.

【図4】原料燃焼時における焼結ベッド上の各層の圧損
を示すグラフである。
FIG. 4 is a graph showing the pressure loss of each layer on the sintering bed during raw material combustion.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 焼結機から排出される排ガスを、再度、
焼結ベッドに戻して焼結原料を焼結する熱源として再使
用する排ガス循環焼結の通気制御方法において、焼結原
料中に、難溶融鉱石を20〜50%配合させたことを特
徴とする排ガス循環焼結通気制御方法。
1. The exhaust gas discharged from the sintering machine,
In the ventilation control method of exhaust gas circulation sintering, which is returned to the sintering bed and reused as a heat source for sintering the sintering raw material, 20 to 50% of refractory ore is mixed in the sintering raw material. Exhaust gas circulation sintering ventilation control method.
JP14558994A 1994-06-03 1994-06-03 Method for controlling permeable gas in exhaust gas circulated sintering Withdrawn JPH07331344A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14558994A JPH07331344A (en) 1994-06-03 1994-06-03 Method for controlling permeable gas in exhaust gas circulated sintering

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14558994A JPH07331344A (en) 1994-06-03 1994-06-03 Method for controlling permeable gas in exhaust gas circulated sintering

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JPH07331344A true JPH07331344A (en) 1995-12-19

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015203151A (en) * 2014-04-16 2015-11-16 株式会社神戸製鋼所 Production method of reduced iron
CN106939373A (en) * 2017-02-23 2017-07-11 首钢京唐钢铁联合有限责任公司 A kind of control method of sintering fuel granularity

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015203151A (en) * 2014-04-16 2015-11-16 株式会社神戸製鋼所 Production method of reduced iron
CN106939373A (en) * 2017-02-23 2017-07-11 首钢京唐钢铁联合有限责任公司 A kind of control method of sintering fuel granularity
CN106939373B (en) * 2017-02-23 2019-02-01 首钢京唐钢铁联合有限责任公司 A kind of control method of sintering fuel granularity

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