JPH10265782A - Production of coke for producing sintered ore and device therefor - Google Patents

Production of coke for producing sintered ore and device therefor

Info

Publication number
JPH10265782A
JPH10265782A JP7363297A JP7363297A JPH10265782A JP H10265782 A JPH10265782 A JP H10265782A JP 7363297 A JP7363297 A JP 7363297A JP 7363297 A JP7363297 A JP 7363297A JP H10265782 A JPH10265782 A JP H10265782A
Authority
JP
Japan
Prior art keywords
coke
rolls
roll crusher
crushing
distance
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Withdrawn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
JP7363297A
Other languages
Japanese (ja)
Inventor
Harumi Ishii
晴美 石井
Yukio Tomita
幸雄 富田
Susumu Kameo
晋 亀尾
Nobuyuki Tsutamoto
信幸 蔦本
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 JP7363297A priority Critical patent/JPH10265782A/en
Publication of JPH10265782A publication Critical patent/JPH10265782A/en
Withdrawn legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Coke Industry (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a coke having the optimal grain size distribution suitable for the production of a sintered ore for blast furnaces in a small fine powder generation ratio by crushing coke with roll crushers in plural stages having small crushing ratios, subsequently. SOLUTION: Rolls 1 having a distance C1 between the rolls 1 and rolls 2 having a distance C2 (C2 <C1 ) between the rolls 2 are vertically disposed. Raw material coke 5 in an ore-storing hopper 3 is ground between rolls 1, and the ground coke having smaller sizes than the distance C1 between the rolls 1 is again ground between rolls 2. In the method, the grinding ratio of each step is small in comparison with that of a single roll crusher, and the coke can be crushed into the same grain size in multi-stages. The generation of fine powder due to the excessive grinding of the coke can be reduced.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明が属する技術分野】本発明は、高炉の主原料であ
る焼結鉱を製造するために用いるコークスの製造方法及
び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing coke used for producing sintered ore, which is a main raw material of a blast furnace.

【0002】[0002]

【従来技術】焼結鉱は、粉鉄鉱石に石灰石等のCaO含
有副原料、珪石や蛇紋岩等のSiO2含有副原料及びコー
クス等を混合し、これに適当な水分を加えて疑似粒化し
たのち、下向き吸引式焼結機のパレット上に装入し、表
層部のコークスに着火後、下方に向けて空気を吸引しな
がらコークスを焼結させ、その燃焼熱により配合原料を
焼結することにより得られるようになっており、コーク
スにはスクリーンで分級した篩下の小中塊のコークスを
ロッドミル粉砕機で粉砕したものを使用している。
BACKGROUND OF THE INVENTION sinter, CaO-containing auxiliary raw materials limestone, etc. fine iron ore, a mixture of SiO 2 containing auxiliary materials and coke such as silica stone and serpentinite, pseudo granulated by adding an appropriate water thereto After that, it is charged on the pallet of the downward suction type sintering machine, and after igniting the coke on the surface layer, the coke is sintered while sucking air downward, and the compounding material is sintered by the heat of combustion. The coke is obtained by crushing small and medium-sized coke under a sieve classified by a screen with a rod mill crusher.

【0003】[0003]

【発明が解決しようとする課題】焼結用コークスは微粉
であると、充填密度が高くなって通気性が低下し、焼成
速度を低下させること、微粉コークスは熱保持力が小さ
く、着火してもすぐに消火してしまうためパレット上の
原料層温度を高温まで昇温させることができず、溶融量
が減少して強度が低下すること、とくに吸引空気による
冷却効果が大きい表層部での強度低下が著しいこと、コ
ークスの熱保持力が小さいため、コークス粒子間の熱伝
播が均一に行われにくゝ、不均一焼成、生焼け部を発生
させ、強度低下を招くことなどの不具合がある。一方、
粒度が大きいと、熱保持力が大きいため、溶融量が増大
し強度を高くするものゝ、融液が過剰生成されて通気性
を阻害し、焼成速度を低下させること、融液の過剰生成
は原料層内に不均一通気をもたらす原因となり、不均一
焼成や生焼け部が発生し、強度低下を招くなどの不具合
を生ずる。
When the coke for sintering is a fine powder, the packing density increases and the permeability decreases, and the sintering speed decreases. The fine coke has a small heat holding power and is ignited. Because the fire extinguishes quickly, the temperature of the raw material layer on the pallet cannot be raised to a high temperature, the amount of melting decreases, and the strength decreases. Due to the remarkable decrease and the low heat retention of coke, heat propagation between coke particles is difficult to perform uniformly, and uneven coking and unburned portions are generated, resulting in problems such as reduced strength. on the other hand,
If the particle size is large, the heat holding power is large, so the amount of melting increases and the strength increases. ゝ The excessive generation of the melt impairs air permeability, lowers the firing rate, and the excessive generation of the melt This causes non-uniform ventilation in the raw material layer, resulting in non-uniform firing and unburned portions, causing problems such as reduction in strength.

【0004】本発明者らは、焼結鉱製造に適したコーク
スの粒度について種々実験を重ねた結果、粒径が0.5
〜5mmのコークスを使用すると、歩留が上がって生産性
が向上することを見い出した。しかしながら従来のロッ
ドミル粉砕機では、0.5〜5mmの適正な粒度分布を有
するコークスを得ることは容易でなく、粒径が5mm以上
の粗粒分が増加したり、0.5mm以下の微粉の割合が増
加しがちである。
The present inventors have conducted various experiments on the particle size of coke suitable for sinter production, and as a result, the coke particle size was 0.5%.
It has been found that the use of ~ 5 mm coke increases yield and improves productivity. However, it is not easy to obtain a coke having an appropriate particle size distribution of 0.5 to 5 mm with a conventional rod mill pulverizer, and coarse particles having a particle size of 5 mm or more increase or fine particles of 0.5 mm or less. The proportion tends to increase.

【0005】本発明者らはそこでロールクラッシャーに
よる破砕を考え、種々実験を行った。その結果、ロール
間の設定した間隔より小さなサイズのものだけが得られ
るばかりでなく、微粉の発生割合も少なくなることを見
出した。本発明は、ロールクラッシャーによる破砕につ
いて更に検討を加えた結果なされたもので、微粉の発生
割合をより少なくすることができるような方法及び装置
を提供することを目的とする。
[0005] The inventors of the present invention conducted various experiments in consideration of crushing by a roll crusher. As a result, it has been found that not only a product having a size smaller than the set interval between the rolls is obtained, but also the generation ratio of fine powder is reduced. The present invention has been made as a result of further study on crushing by a roll crusher, and an object of the present invention is to provide a method and an apparatus capable of further reducing the generation rate of fine powder.

【0006】[0006]

【課題の解決手段】本発明の方法は、ロールクラッシャ
ーによるコークスの破砕を各段階での破砕比を少なくし
て数段階で行うことを特徴とする。本発明で用いるロー
ルクラッシャーは、ロール間の間隔が異なる複数のロー
ルクラッシャーよりなっていてもよいが、好ましくは間
隔の異なるロールを複数組設けた一つのロールクラッシ
ャーが用いられる。
The method of the present invention is characterized in that the crushing of coke by a roll crusher is performed in several stages with a reduced crushing ratio in each stage. The roll crusher used in the present invention may be composed of a plurality of roll crushers with different intervals between the rolls, but preferably one roll crusher provided with a plurality of sets of rolls with different intervals is used.

【0007】本発明の装置は、上記の方法を実施するた
めの装置で、下方に向かってロール間の間隔を狭くした
複数組のロールを縦方向に設置したロールクラッシャー
よりなるものである。
[0007] The apparatus of the present invention is an apparatus for performing the above-mentioned method, and comprises a roll crusher in which a plurality of sets of rolls having a narrower interval between rolls are installed vertically in a downward direction.

【0008】[0008]

【発明の実施の形態】図1は、本発明に係わるロールク
ラッシャーの概念図を示すもので、ロール間の間隔C1
のロール1と、間隔C2 (C2 <C1 )のロール2を上
下に配置すると共に、ロール1上に貯鉱ホッパー3を、
ロール1、2間にホッパー4を設け、貯鉱ホッパー3内
の原料コークス5を先ず上段のロール1間で破砕する。
このときロール間の間隔C1 より小さなサイズのコーク
スの大半は破砕されることなく排出され、ホッパー4内
に投下する。次にC1 よりサイズの小さなホッパー4内
のコークスが下段のロール2間でロール間の間隔C2
り小さなサイズに破砕される。このときも同様、ロール
間の間隔C2 より小さなサイズのコークスの大半は破砕
されることなく排出される。
Figure 1 DETAILED DESCRIPTION OF THE INVENTION, shows a conceptual diagram of a roll crusher according to the present invention, distance C 1 between rolls
Roll 1 and a roll 2 with an interval C 2 (C 2 <C 1 ) are arranged vertically, and a storage hopper 3 is placed on the roll 1,
A hopper 4 is provided between the rolls 1 and 2, and the raw coke 5 in the ore storage hopper 3 is first crushed between the upper rolls 1.
Most of the coke size smaller than the interval C 1 between the time rolls is discharged without being crushed, to drop into the hopper 4. Then coke small hopper 4 size than C 1 is crushed to a smaller size than the distance C 2 between rolls between the lower roll 2. Similarly this time, most of the coke size smaller than the distance C 2 between the rolls is discharged without being crushed.

【0009】次に上記ロールクラッシャーによる破砕比
について具体的に説明する。ロール1間の間隔C1 を1
0mm、ロール2間の間隔C2 を3mmに設定すると、貯鉱
ホッパー3内の30mm以下の粒径の原料コークス5のう
ち、最大径30mmのコークスがロール1において破砕比
30/10=3/1で破砕され、ついでロール2におい
て最大径10mmのコークスが破砕比10/3=3.3/
1で破砕される。
Next, the crushing ratio by the roll crusher will be specifically described. The distance C 1 between the roll 1 1
0 mm, by setting the distance C 2 between rolls 2 to 3 mm, of the feed coke 5 below the diameter 30mm in貯鉱hopper 3, crushing ratio maximum diameter 30mm coke in the roll 1 30/10 = 3 / Coke having a maximum diameter of 10 mm on the roll 2 at a crushing ratio of 10/3 = 3.3 /
Crushed in 1.

【0010】一方、一組のロールを用いた単装ロールク
ラッシャーで、ロール間の間隔を3mmに設定して同じ原
料コークスから同じ粒度のものを得ようとすると、最大
径3mmのコークスは破砕比30/3=10/1で破砕さ
れるようになり、粉々に過剰粉砕されるようになる。
[0010] On the other hand, when a single roll crusher using a set of rolls is used to set the distance between the rolls to 3 mm to obtain the same raw material coke having the same particle size, the coke having a maximum diameter of 3 mm is crushed. Crushed at 30/3 = 10/1, resulting in excessive pulverization.

【0011】[0011]

【実施例】【Example】

実施例1 図1に示すタイプのロールクラッシャーを用い、ロール
1間の間隔C1 を5mm、ロール2間の間隔C2 を3mmに
設定して粒径10〜15mmの原料コークスを破砕した。
その結果得られた製品コークスには0.5mm以下の微粉
コークスは約17%であった。因みに単装式のロールク
ラッシャーを用い、ロール間の間隔を3mmに設定して上
記と同じ原料コークスを1回で破砕した。その結果得ら
れた製品コークスには、0.5mm以下の微粉コークスが
約21%となった。
Example 1 A raw coke having a particle size of 10 to 15 mm was crushed by using a roll crusher of the type shown in FIG. 1 and setting the interval C1 between the rolls 1 to 5 mm and the interval C2 between the rolls 2 to 3 mm.
The resulting product coke contained about 17% fine coke less than 0.5 mm. Incidentally, the same raw coke as above was crushed at one time by using a single-mounted roll crusher and setting the interval between the rolls to 3 mm. The resulting product coke contained about 21% fine coke of 0.5 mm or less.

【0012】実施例2 ロール1間の間隔C1 を10mm、ロール2間の間隔C2
を5mmに設定し、実施例1と同じ粒径10〜15mmの原
料コークスを破砕した。その結果得られた製品コークス
の粒度分布を図2の白丸で示す。因みに単装式のロール
クラッシャーにおいて、ロール間隔を5mmに設定して同
じコークスを1回で破砕した。その結果得られた製品コ
ークスの粒度分布を図の黒丸で示す。
[0012] Example 2 10 mm spacing C 1 between the roll 1, the distance C 2 between rolls 2
Was set to 5 mm, and the raw material coke having the same particle diameter of 10 to 15 mm as in Example 1 was crushed. The particle size distribution of the resulting product coke is indicated by white circles in FIG. Incidentally, the same coke was crushed once by using a single-mounted roll crusher with the roll interval set to 5 mm. The particle size distribution of the resulting product coke is indicated by black circles in the figure.

【0013】上記各実施例に示されるように、大きな破
砕比で1回で破砕するよりも破砕比を小さくして2回で
破砕する方が0.5mm以下の微粉の割合が減少した。
As shown in the above examples, the ratio of fine powder having a size of 0.5 mm or less decreased when the crushing ratio was reduced and crushed twice, rather than crushed once with a large crushing ratio.

【0014】[0014]

【発明の効果】請求項1記載の発明によると、ロール間
の間隔を設定することにより設定粒度以下のものが確実
に得られるようになるうえ、ロールクラッシャーによる
破砕が数段階で行われ、1回の破砕比が小さくなるため
過剰粉砕がなくなり、微粉の発生割合も少なくなる。
According to the first aspect of the present invention, by setting the interval between the rolls, it is possible to surely obtain particles having a particle size equal to or less than the set particle size, and crushing by a roll crusher is carried out in several stages, and Since the crushing ratio per time is reduced, excessive pulverization is eliminated, and the generation ratio of fine powder is reduced.

【0015】請求項2又は3記載の発明によると、単一
のロールクラッシャーにより微粉の発生割合の少ない製
品コークスを得ることができる。
According to the second or third aspect of the present invention, it is possible to obtain a product coke with a low generation rate of fine powder by a single roll crusher.

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

【図1】本発明に係わるロールクラッシャーの概略図。FIG. 1 is a schematic view of a roll crusher according to the present invention.

【図2】単装式と連装式のロールクラッシャーを用いて
得られた製品コークスの粒度分布を示すグラフ。
FIG. 2 is a graph showing the particle size distribution of product coke obtained by using a single-type and a multiple-type roll crusher.

【符号の説明】[Explanation of symbols]

1、2・・ロール 3・・貯鉱ホッパー 4・・ホッパー 5・・コークス 1, 2, roll 3, storage hopper 4, hopper 5, coke

フロントページの続き (72)発明者 蔦本 信幸 広島県呉市昭和町11番1号 日新製鋼株式 会社呉製鉄所内Continued on the front page (72) Inventor Nobuyuki Tatsumoto 11-1 Showa-cho, Kure-shi, Hiroshima Nisshin Steel Co., Ltd. Kure Works

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】高炉用焼結鉱を製造するために用いられる
最適粒度分布のコークスを製造する方法において、ロー
ルクラッシャーによるコークスの破砕を各段階での破砕
比を少なくして数段階で行うことを特徴とする焼結鉱製
造用コークスの製造方法。
1. A method for producing coke having an optimum particle size distribution used for producing sintered ore for a blast furnace, wherein the crushing of coke by a roll crusher is performed in several stages with a reduced crushing ratio in each stage. A method for producing coke for producing sintered ore, characterized by the following.
【請求項2】上記ロールクラッシャーは複数組のロール
を縦方向に設置した連装式のロールクラッシャーである
請求項1記載の焼結鉱製造用コークスの製造方法。
2. The method according to claim 1, wherein the roll crusher is a continuous roll crusher in which a plurality of sets of rolls are installed in a vertical direction.
【請求項3】請求項2記載の方法を実施するための装置
で、下方に向かってロール間の間隔を狭くした複数組の
ロールを縦方向に設置したロールクラッシャーよりなる
装置。
3. An apparatus for carrying out the method according to claim 2, comprising a roll crusher in which a plurality of sets of rolls having a narrower interval between rolls are installed vertically in a downward direction.
JP7363297A 1997-03-26 1997-03-26 Production of coke for producing sintered ore and device therefor Withdrawn JPH10265782A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7363297A JPH10265782A (en) 1997-03-26 1997-03-26 Production of coke for producing sintered ore and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7363297A JPH10265782A (en) 1997-03-26 1997-03-26 Production of coke for producing sintered ore and device therefor

Publications (1)

Publication Number Publication Date
JPH10265782A true JPH10265782A (en) 1998-10-06

Family

ID=13523889

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7363297A Withdrawn JPH10265782A (en) 1997-03-26 1997-03-26 Production of coke for producing sintered ore and device therefor

Country Status (1)

Country Link
JP (1) JPH10265782A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000056457A1 (en) * 1999-03-18 2000-09-28 Psp Engineering, A.S. Method for milling of material with large range of grindability
CN104107804A (en) * 2013-02-26 2014-10-22 刘晓 Wind-force-controllable dressing system for nonferrous metallic ores and rare nonmetallic ores
KR101480873B1 (en) * 2012-12-28 2015-01-09 주식회사 포스코 Apparatus and control method for crushing with uniform size coke using in sintering process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000056457A1 (en) * 1999-03-18 2000-09-28 Psp Engineering, A.S. Method for milling of material with large range of grindability
KR101480873B1 (en) * 2012-12-28 2015-01-09 주식회사 포스코 Apparatus and control method for crushing with uniform size coke using in sintering process
CN104107804A (en) * 2013-02-26 2014-10-22 刘晓 Wind-force-controllable dressing system for nonferrous metallic ores and rare nonmetallic ores

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