JP2000290732A - Granulation method of raw materials for sintering with excellent flammability - Google Patents

Granulation method of raw materials for sintering with excellent flammability

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Publication number
JP2000290732A
JP2000290732A JP11097771A JP9777199A JP2000290732A JP 2000290732 A JP2000290732 A JP 2000290732A JP 11097771 A JP11097771 A JP 11097771A JP 9777199 A JP9777199 A JP 9777199A JP 2000290732 A JP2000290732 A JP 2000290732A
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JP
Japan
Prior art keywords
coke
sintering
drum mixer
ore
particles
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.)
Granted
Application number
JP11097771A
Other languages
Japanese (ja)
Other versions
JP4087982B2 (en
Inventor
Kenichi Yatsugayo
健一 八ケ代
Takeshi Imai
武 今井
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
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Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP09777199A priority Critical patent/JP4087982B2/en
Publication of JP2000290732A publication Critical patent/JP2000290732A/en
Application granted granted Critical
Publication of JP4087982B2 publication Critical patent/JP4087982B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

(57)【要約】 【課題】 焼結機内の擬似粒子の燃焼性を良好にし、焼
結鉱の生産性や歩留り等を向上することができる燃焼性
に優れた焼結用原料の造粒方法を提供する。 【解決手段】 ドラムミキサー11に粉鉱石とコークス
を添加して攪拌を行って擬似粒子に造粒する焼結用原料
の造粒方法において、予め粉鉱石に全添加量の20〜5
0重量%のコークスを添加し、残部のコークスを、ドラ
ムミキサー11の全長をLとして、装入口から0.5L
〜0.98Lの範囲に添加する。
PROBLEM TO BE SOLVED: To provide a method for granulating a raw material for sintering having excellent flammability capable of improving flammability of pseudo particles in a sintering machine and improving productivity and yield of sinter. I will provide a. SOLUTION: In a granulation method of a raw material for sintering in which fine ore and coke are added to a drum mixer 11 and agitated to granulate into pseudo-particles, the total amount of the fine ore is 20 to 5 in advance.
0% by weight of coke was added, and the remaining coke was added to the drum mixer 11 with the total length of L as 0.5 L from the charging inlet.
Add to the range of 0.90.98 L.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、粉鉱石等にコーク
スを添加し擬似粒子に造粒して焼結鉱を製造する際に、
擬似粒子の燃焼性を高めて生産性を向上する焼結用原料
の造粒方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing sintered ore by adding coke to fine ore and granulating into pseudo particles.
The present invention relates to a method for granulating a raw material for sintering, which enhances the flammability of pseudo particles and improves productivity.

【0002】[0002]

【従来の技術】一般に製鉄原料は、8mm以下の微粉の
鉄鉱石や集塵機等から回収されたダスト、焼結機から払
い出された後の篩下粉(返し鉱)等の粉鉱石に、コーク
スを添加し、水や生石灰等のバインダーを添加して、ド
ラムミキサー等を用いて擬似粒子を造粒し、これを焼結
機に装入して1100〜1300℃の温度で焼いて焼結
鉱を製造し、高炉に使用している。この焼結鉱の品質
は、高炉の通気性や装入の荷下がり等に影響し、場合に
よっては、高炉の安定操業や高炉の出銑量等に支障が生
じる場合があり、良質の焼結鉱の供給が望まれている。
また、焼結機により製造される焼結鉱は、微粉を多く含
んだ粉鉱石等とコークスを添加して造粒した擬似粒子の
良否によって、焼結操業時の通気性や燃焼性、擬似粒子
の焼結状態に影響を与え、その強度や還元粉化率(RD
I)等の特性が大きく左右され、これ等の品質と生産性
や焼結歩留りを満足する擬似粒子の製造そのものが難し
い実情であった。従って、旧来より焼結鉱の品質や生産
性、焼結歩留り等を向上するために、特開昭63−69
926号公報に記載されているように、微粉の鉄鉱石や
返し鉱等の粉鉱石に、全使用水の40〜90重量%の水
を添加してドラムミキサー等で混合して、最初に粉鉱石
のみからなる擬似粒子を製造し、この擬似粒子にコーク
スやスケール等の副原料を加えてドラムミキサー等を用
いて、内部の鉄分からなる粒子の表面にコークスの付着
層を形成することにより、焼結機での着火性及び燃焼性
を改善して焼結鉱の生産性を向上している。また、特開
昭62−225238号公報に記載されているように、
粉鉱石や石灰石等の原料をドラムミキサー内に装入し、
ドラムミキサー内の原料の運動領域に噴霧管から擬似粒
子化促進剤を添加して擬似粒子を製造し、焼結機での通
気性の改善や燃焼時間の短縮等により、焼結鉱の生産性
を向上することが行われている。
2. Description of the Related Art Generally, iron ore raw materials are coke fines such as fine iron ore having a size of 8 mm or less, dust collected from dust collectors, and undersize sieves (reclaimed ore) discharged from a sintering machine. Is added, a binder such as water or quicklime is added, and pseudo particles are granulated using a drum mixer or the like, and this is charged into a sintering machine and baked at a temperature of 1100 to 1300 ° C. Is manufactured and used in blast furnaces. The quality of the sinter affects the air permeability of the blast furnace and the unloading of the blast furnace, and in some cases, the stable operation of the blast furnace and the output of the blast furnace may be hindered. Supply of ore is desired.
In addition, the sinter produced by the sintering machine depends on the quality of pseudo-particles obtained by adding fine ore and coke and granulating by adding coke. Affects the sintering state of the steel, its strength and reduced powdering ratio (RD
The properties such as I) are greatly affected, and it has been difficult to produce pseudo particles which satisfy these qualities, productivity and sintering yield. Therefore, in order to improve the quality and productivity of sinter, sintering yield, etc.
As described in Japanese Patent Publication No. 926, a water ore of 40 to 90% by weight of total use water is added to fine ore such as iron ore or rock ore and mixed with a drum mixer or the like, and the powder is firstly mixed. By producing pseudo-particles consisting only of ore, adding auxiliary materials such as coke and scale to the pseudo-particles and using a drum mixer or the like to form an adhesion layer of coke on the surface of the particles composed of iron inside, The ignitability and flammability in the sintering machine have been improved to improve the productivity of sinter. Further, as described in JP-A-62-225238,
Raw materials such as fine ore and limestone are charged into a drum mixer,
A quasi-particle is produced by adding a quasi-particle forming accelerator from a spray pipe to a moving region of the raw material in a drum mixer, and sinter ore productivity is improved by improving air permeability in a sintering machine and shortening combustion time. Improvements have been made.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、特開昭
63−69926号公報では、内部の鉄分をリッチにし
た擬似粒子の表面にコークスの付着層を形成しているの
で、焼結機に装入した際に、着火性及び燃焼性が良好に
なり過ぎて、燃焼速度が過剰に上昇し、上層から下層に
おける燃焼帯の移動が速くなり、コークスの少ない内部
に十分な熱を付与することができず、内部の焼結が不十
分になったり、粒子間におけるボンドの形成が悪くな
る。その結果、焼結鉱の強度の低下を招き、高炉への搬
送過程や高炉内に装入した際に粉化し、高炉の通気性等
を阻害して出銑量の低下等が生じる。また、特開昭62
−225238号公報では、ドラムミキサー内を転動し
ながら粉鉱石やコークス等が擬似粒子になりつつある運
動領域内に噴霧管から擬似粒子化促進剤を添加して擬似
粒子にするので、コークスがほぼ均等に含まれる擬似粒
子になり、焼結機内の疑似粒子の燃焼性が阻害され、生
産性や歩留りが低下する等の問題がある。
However, according to Japanese Patent Application Laid-Open No. 63-69926, an adhesion layer of coke is formed on the surface of the pseudo-particles in which the iron content is enriched. In this case, the ignitability and flammability become too good, the combustion speed rises excessively, the movement of the combustion zone from the upper layer to the lower layer becomes faster, and sufficient heat can be given to the inside with less coke. In addition, the internal sintering becomes insufficient and the formation of bonds between the particles becomes poor. As a result, the strength of the sintered ore is reduced, and the sintered ore is pulverized during the transportation process to the blast furnace or charged in the blast furnace, impairing the air permeability of the blast furnace and reducing the tapping amount. In addition, Japanese Unexamined Patent Publication
According to JP-A-225238, pseudo-particulation accelerator is added from a spray pipe into pseudo-particles in a motion region where fine ore or coke is turning into pseudo-particles while rolling in a drum mixer. Pseudo-particles are included almost uniformly, and the flammability of the pseudo-particles in the sintering machine is impaired, and there are problems such as a decrease in productivity and yield.

【0004】本発明はかかる事情に鑑みてなされたもの
で、焼結機内の擬似粒子の燃焼性を良好にし、焼結鉱の
生産性や歩留り等を向上することができる燃焼性に優れ
た焼結用原料の造粒方法を提供することを目的とする。
[0004] The present invention has been made in view of the above circumstances, and a sinter having excellent flammability capable of improving the flammability of pseudo particles in a sintering machine and improving the productivity and yield of sintered ore. It is an object of the present invention to provide a method for granulating a binding raw material.

【0005】[0005]

【課題を解決するための手段】前記目的に沿う本発明に
係る燃焼性に優れた焼結用原料の造粒方法は、ドラムミ
キサーで粉鉱石とコークスを攪拌して擬似粒子に造粒す
る焼結用原料の造粒方法において、予め前記コークスの
全添加量の20〜50重量%と前記粉鉱石とを前記ドラ
ムミキサーに装入し、残部のコークスを、前記ドラムミ
キサーの全長をLとして装入口から0.5L〜0.98
Lの範囲に添加する。この方法により、擬似粒子の内部
と表層にコークスを含ませ、表層に露出するコークスが
多くなり、装入した擬似粒子の着火性及び燃焼性が高ま
り、表層の燃焼速が向上し、内部を温度の上昇につれて
燃焼させることができ、燃焼性を向上させながら相反す
る燃焼速度を適正にできる。なお、残部のコークスを添
加する位置がドラムミキサーの0.5Lより手前の範囲
になると、擬似粒子の内部のコークスが増加したり、コ
ークスそのものの表面に粉鉱石が付着して、疑似粒子の
燃焼性が低下したり、燃焼速度が遅くなり、焼結鉱の強
度や生産性等が阻害される。一方、ドラムミキサーの
0.98Lより後方(留時間が10秒未満)になると、
擬似粒子の表面に付着するコークスが少なくなり、擬似
粒子に必要なコークスの絶対量が不足し、燃焼性や燃焼
速度が低下する。
According to the present invention, there is provided a method for granulating a raw material for sintering having excellent flammability according to the present invention, which comprises mixing fine ore and coke with a drum mixer to granulate into pseudo particles. In the method for granulating the binding raw material, 20 to 50% by weight of the total amount of the coke and the fine ore are charged into the drum mixer in advance, and the remaining coke is charged with the total length of the drum mixer being L. 0.5L ~ 0.98 from the entrance
Add to L range. By this method, coke is contained in the inside and the surface layer of the pseudo particles, the coke exposed to the surface layer increases, the ignitability and flammability of the charged pseudo particles are increased, the burning speed of the surface layer is improved, and the inside temperature is increased. Can be burned as the temperature rises, and contradictory burning speeds can be made appropriate while improving flammability. When the position where the remaining coke is added is within a range of 0.5 L before the drum mixer, the coke inside the pseudo particles increases, or fine ore adheres to the surface of the coke itself, and the pseudo particles burn. The sinter ore strength and productivity, etc. are impaired due to a reduction in the burnability and a decrease in the burning rate. On the other hand, if it is later than 0.98 L of the drum mixer (residence time is less than 10 seconds),
The amount of coke adhering to the surface of the pseudo particles is reduced, the absolute amount of coke required for the pseudo particles is insufficient, and the combustibility and the burning speed are reduced.

【0006】ここで、前記粉鉱石は、粒度が500μm
未満の微粉を30〜70重量%含んでいる。これによ
り、添加したコークスが、最初に造粒された擬似粒子や
その外側に形成される層の内部に埋もれて、燃焼性や燃
焼速度が悪くなるのを防止できる。500μm未満の粉
鉱石が70重量%を超えると、微粉が多くなり過ぎて、
最初の擬似粒子の形成が悪くなり、後で添加する残部の
コークスに粉鉱石が付着して燃焼性等を阻害する。50
0μm未満の粉鉱石が30重量%未満になると、擬似粒
子内へのコークスの混入やコークス表面への粉鉱石の付
着が減少し、コークス添加を前後に分割する効果が無く
なる。
The fine ore has a particle size of 500 μm.
Less than 30 to 70% by weight of fine powder. Thereby, it is possible to prevent the added coke from being buried in the pseudo-particles initially granulated or in the layer formed on the outer side thereof, thereby deteriorating the combustibility and the burning speed. If the fine powder ore having a particle size of less than 500 μm exceeds 70% by weight, the fine powder becomes too large,
The formation of pseudo particles at the beginning deteriorates, and fine ore adheres to the remaining coke to be added later, thereby impairing combustibility and the like. 50
When the amount of the fine ore having a particle size of less than 0 μm is less than 30% by weight, the mixing of coke into the pseudo particles and the adhesion of the fine ore to the coke surface are reduced, and the effect of dividing the coke addition into front and rear ends.

【0007】更に、前記残部のコークスの添加位置を、
500μm未満の粉鉱石の含有量に応じて調整すること
ができる。これにより、最初に造粒された擬似粒子の状
態に適したコークスを適正な位置で添加し、擬似粒子の
内部に含まれるコークスを均一にし、表層に付着するコ
ークスを多くでき、燃焼性や燃焼速度をより安定させる
ことができる。
Further, the addition position of the remaining coke is
It can be adjusted according to the content of fine ore less than 500 μm. As a result, coke suitable for the state of the pseudo-particles initially granulated is added at an appropriate position, the coke contained in the pseudo-particles is made uniform, the coke adhering to the surface layer can be increased, and the combustibility and combustion can be increased. Speed can be made more stable.

【0008】[0008]

【発明の実施の形態】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の形態につき説明し、本発
明の理解に供する。図1は本発明の一実施の形態に係る
燃焼性に優れた焼結用原料の造粒方法に適用される焼結
用原料の造粒装置の全体図、図2は同造粒方法に適用す
る粉鉱石とコークスの粒径ごとの容積%を比較したグラ
フ、図3は粉鉱石中の500μm未満の粉鉱石の重量%
とコークス付着厚を200μmとするコークスの添加位
置の関係を示すグラフ、図4はコークスの付着厚と焼結
機の生産性の関係を示すグラフである。図1に示すよう
に、本発明の一実施の形態に係る燃焼性に優れた焼結用
原料の造粒方法に用いられる焼結用原料の造粒装置10
は、図示しない駆動装置により傾斜状態で回転するドラ
ムミキサー11と、このドラムミキサー11内に微粉の
鉄鉱石、返し鉱石、ダスト等の粉鉱石を貯蔵する貯蔵ホ
ッパー12及び貯蔵ホッパー12から粉鉱石を切り出す
フィーダ13と、コークスの貯蔵ホッパー14及び貯蔵
ホッパー14からコークスを切り出すフィーダ15と、
これ等の粉鉱石とコークスを搬送するベルトコンベア1
6、17と、後からドラムミキサー11にコークスを添
加するためのベルトコンベア18、その上方に設けられ
たコークスの貯蔵ホッパー19及びフィーダ20とを備
えている。更に、ドラムミキサー11の入り側には、装
入される粉鉱石に散水するスプレー配管21を備えてお
り、ドラムミキサー11の出側には、ドラムミキサー1
1からでた擬似粒子を分級する篩22を設けている。こ
の篩22の篩上は、製品として図示しない焼結機に搬送
され、篩下となる返し粉23は、ベルトコンベア17に
返送して再度ドラムミキサー11に供給している。な
お、ここで、Lは、ドラムミキサー11の全長を表す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the accompanying drawings to provide an understanding of the present invention. FIG. 1 is an overall view of an apparatus for granulating a raw material for sintering which is applied to a method for granulating a raw material for sintering having excellent flammability according to an embodiment of the present invention, and FIG. FIG. 3 is a graph comparing the volume% of fine ore and the coke for each particle size, and FIG. 3 shows the weight% of fine ore of less than 500 μm in the fine ore.
And FIG. 4 is a graph showing the relationship between the coke deposition thickness and the productivity of the sintering machine when the coke deposition thickness is set to 200 μm. As shown in FIG. 1, a sintering raw material granulating apparatus 10 used in a method for granulating a sintering raw material excellent in combustibility according to one embodiment of the present invention.
Is a drum mixer 11 that rotates in an inclined state by a driving device (not shown), a storage hopper 12 that stores fine ore such as fine iron ore, return ore, and dust in the drum mixer 11, and fine ore from the storage hopper 12. A feeder 13 for cutting, a storage hopper 14 for coke, and a feeder 15 for cutting coke from the storage hopper 14;
Belt conveyor 1 for transporting these fine ores and coke
6, a belt conveyor 18 for adding coke to the drum mixer 11 later, and a coke storage hopper 19 and a feeder 20 provided thereabove. Further, on the inlet side of the drum mixer 11, there is provided a spray pipe 21 for sprinkling water to the charged ore, and on the outlet side of the drum mixer 11, a drum mixer 1 is provided.
A sieve 22 is provided for classifying the pseudo particles obtained from Step 1. The top of the sieve 22 is conveyed as a product to a sintering machine (not shown), and the returned powder 23 to be sieved is returned to the belt conveyor 17 and supplied to the drum mixer 11 again. Here, L represents the total length of the drum mixer 11.

【0009】次に、焼結用原料の造粒装置10を用いた
燃焼性に優れた焼結用原料の造粒方法について説明す
る。まず、貯蔵ホッパー12に貯蔵された微粉の鉄鉱
石、返し鉱石、ダスト等からなる粉鉱石は、6mm以下
の大きさであり、特に粒度500μm未満(−500μ
m)の微粉を30〜70重量%含有している。貯蔵ホッ
パー14に貯蔵されたコークスは、6mm以下各粒度が
略平均的に分布している。この粉鉱石及びコークスは、
フィーダ13、15からベルトコンベア16上に切り出
され、ベルトコンベア17に乗り継いでドラムミキサー
11内に装入される。最終的に粉鉱石に対するコークス
の全配合量(全添加量)は、2.5重量%であり、この
内の20〜50重量%がここで貯蔵ホッパー14から切
り出されることになる。そして、残部のコークスは、ド
ラムミキサー11の装入口から0.5L〜0.98Lの
範囲で、貯蔵ホッパー19からフィーダ20、ベルトコ
ンベア18を介して添加される。
Next, a method of granulating a raw material for sintering having excellent flammability using the granulating apparatus 10 for raw material for sintering will be described. First, the fine ore composed of fine iron ore, turning ore, dust, and the like stored in the storage hopper 12 has a size of 6 mm or less, and particularly has a particle size of less than 500 μm (−500 μm).
30) to 70% by weight of the fine powder of m). The coke stored in the storage hopper 14 has a particle size of 6 mm or less, and each particle size is substantially averagely distributed. This fine ore and coke
The paper is cut out from the feeders 13 and 15 onto the belt conveyor 16, transferred to the belt conveyor 17 and loaded into the drum mixer 11. Finally, the total blended amount of coke to the fine ore (total added amount) is 2.5% by weight, of which 20 to 50% by weight is cut out from the storage hopper 14 here. Then, the remaining coke is added from the storage hopper 19 through the feeder 20 and the belt conveyor 18 within a range of 0.5 L to 0.98 L from the charging inlet of the drum mixer 11.

【0010】また、図2のように、粉鉱石に添加するコ
ークス(△)の各粒径(μm)の分布は、6mm〜12
5μmの範囲で略平均的に分布をしている。しかも、粉
鉱石に配合したコークスのみの容積%でみると、添加量
が少ないにも係わらず1.5〜5容積%(平均約3.8
容積%)であり、重量から見た場合にくらべ1.5倍の
容積を有し、コークスの添加量が少なくても擬似粒子の
表面を覆うに十分な量であることが判る。なお、図中□
は、粉鉱物とコークスを配合した場合の粒径分布を示
す。しかし、このコークスは粉鉱石に含有する500μ
m以上の粒子が多くなったり、ドラムミキサー11の装
入側から0.5L未満の範囲に残部のコークスを添加し
た場合では、コークスの内の大きい粒子が核になり、こ
の周囲に粉鉱石が付着した擬似粒子を形成したり、粉鉱
石の擬似粒子の内部に埋没するコークスが多くなったり
して、燃焼性を高めた擬似粒子を得ることができない。
Further, as shown in FIG. 2, the distribution of each particle size (μm) of coke (△) added to the fine ore ranges from 6 mm to 12 mm.
The distribution is approximately average in the range of 5 μm. In addition, in terms of the volume% of only coke blended in the fine ore, 1.5 to 5 volume% (average of about 3.8) despite the small amount of coke added.
% By volume, which is 1.5 times the volume in terms of weight, indicating that even if the amount of coke added is small, it is sufficient to cover the surface of the pseudo particles. In the figure, □
Shows the particle size distribution when powdered mineral and coke are blended. However, this coke contains 500μ
m or more, or when the remaining coke is added in a range of less than 0.5 L from the charging side of the drum mixer 11, large particles in the coke become nuclei, and fine ore is surrounded by the core. Pseudo-particles that have adhered or coke buried inside the pseudo-particles of fine ore increase, so that pseudo-particles with enhanced flammability cannot be obtained.

【0011】従って、予め粉鉱石に全添加量の20〜5
0重量%のコークスと生石灰、石灰石等を添加し、スプ
レー配管21から5〜8重量%の水を散水してからドラ
ムミキサー11で攪拌し、粉鉱石とコークスを混合し、
内部にコークスを含む擬似粒子を造粒する。予め粉鉱石
に添加するコークスの量が20重量%未満になると、擬
似粒子の内部のコークスが不足して、燃焼速度や燃焼温
度を高く保持する時間が短くなり、粒子間のボンドの形
成や焼結不良等が生じる。また、コークスの量が50重
量%を超えると、ドラムミキサー11により造粒された
擬似粒子の内部のコークスが多くなり、表面に付着させ
るコークスの量が減少するので、燃焼性や燃焼速度が低
下し、焼結鉱の歩留りの低下、焼結鉱の強度や還元粉化
率等の品質低下を招くことになる。更に、コークスの各
粒径(μm)が略平均的に分布をしていることを利用し
て、図3に示すように、粉鉱石に含まれる500μm未
満の粒子の量が30重量%の場合で、ドラムミキサー1
1の全長Lに対し、出側方向の0.5Lの位置でコーク
スを添加することで、擬似粒子の表面に200μmの厚
みのコークスを主にした付着層を形成することができ
る。このコークスを主にした付着層は、粉鉱石に含まれ
る500μm未満の粒子の量に応じて、ドラムミキサー
11内のコークスの添加位置を調整することにより、擬
似粒子の表面への付着厚みを100〜250μmとする
ことができ、その一部が露出した形態を有する理想的な
擬似粒子にすることができる。この調整は、粉鉱石とコ
ークスを同じ条件にして、コークスの添加位置を変えな
がら造粒した擬似粒子の表面に付着したコークスの厚み
を測定しておき、図示しない焼結機のパレットの装入の
層厚や焼結機の移動速度等が変動した際に、前記の測定
された値から、コークスの添加位置を変えて付着厚みを
100〜250μmの範囲内で最適な生産性が得られる
ように調整することができる。コークスの添加位置は、
ベルトコンベア18をドラムミキサー11内に進退させ
て位置を決定し、貯蔵ホッパー19のフィーダ20を作
動してコークスの切り出しと搬送を行って、造粒されて
いる粉鉱石に添加する。この残部のコークスの添加量
は、全添加量の50〜80重量%にすることで、擬似粒
子の表面にコークスの100〜250μmの付着層が形
成される。ドラムミキサー11に添加する残部のコーク
スの量が50重量%未満になると、擬似粒子の内部のコ
ークスが増加したり、コークスそのものの表面に粉鉱石
原料が付着が増加して、擬似粒子の燃焼性や燃焼速度が
低下する。しかも、ドラムミキサー11に添加する残部
のコークスの量が80重量%を超えると、擬似粒子の表
面に付着するコークスの量が多くなり、燃焼速度が速く
なり過ぎたり、擬似粒子の内部のコークスの量が不足
し、焼結鉱の品質を阻害するからである。このように、
擬似粒子の表面に積極的にコークスの付着層を形成し、
その付着厚みを100〜250μmに調整することによ
り、図4に示すように、焼結機の生産性(T/d・m
2 )を約29.7〜33に向上することができる。そし
て、ドラムミキサー11を出た擬似粒子は、篩22で分
級され、10mm以上の篩上は焼結機に搬送され、10
mm未満の篩下は、返し粉23として再度ドラムミキサ
ー11に供給される。
[0011] Accordingly, the total amount of 20 to 5
0% by weight of coke and quick lime, limestone, etc. are added, 5 to 8% by weight of water is sprinkled from the spray pipe 21 and then stirred with the drum mixer 11 to mix fine ore and coke,
Pseudo particles containing coke inside are granulated. If the amount of coke to be added to the fine ore in advance is less than 20% by weight, the coke inside the pseudo-particles becomes insufficient, and the time for keeping the combustion speed and the combustion temperature high becomes short, and the formation and burning of bonds between the particles will be shortened. Defective results etc. occur. Further, when the amount of coke exceeds 50% by weight, the amount of coke inside the pseudo particles granulated by the drum mixer 11 increases, and the amount of coke attached to the surface decreases, so that the combustibility and the burning speed decrease. However, the yield of the sintered ore is reduced, and the quality of the sintered ore, such as the strength and the reduction pulverization rate, is reduced. Furthermore, utilizing the fact that the particle diameters (μm) of the coke are substantially averagely distributed, as shown in FIG. 3, the amount of particles less than 500 μm contained in the fine ore is 30% by weight. And drum mixer 1
By adding coke at a position of 0.5 L in the exit side with respect to the total length L of 1, an adhesion layer mainly composed of coke having a thickness of 200 μm can be formed on the surface of the pseudo particles. The adhesion layer mainly composed of coke can adjust the addition position of coke in the drum mixer 11 in accordance with the amount of particles less than 500 μm contained in the fine ore to reduce the adhesion thickness of the pseudo particles to the surface by 100%. To 250 μm, and an ideal pseudo particle having a partially exposed form can be obtained. In this adjustment, the thickness of the coke adhering to the surface of the granulated pseudo-particles was measured while changing the coke addition position under the same conditions of the fine ore and the coke, and the pallet of a sintering machine (not shown) was charged. When the layer thickness or the moving speed of the sintering machine fluctuates, the optimum productivity can be obtained within the range of 100 to 250 μm by changing the coke addition position from the above measured values and changing the coke addition position. Can be adjusted. Coke addition position
The belt conveyor 18 is advanced and retracted into the drum mixer 11 to determine the position, and the feeder 20 of the storage hopper 19 is operated to cut and convey the coke to be added to the granulated fine ore. By setting the addition amount of the remaining coke to 50 to 80% by weight of the total addition amount, an adhesion layer of 100 to 250 μm of coke is formed on the surface of the pseudo particles. If the amount of the remaining coke added to the drum mixer 11 is less than 50% by weight, the coke inside the pseudo particles increases, or the fine ore raw material adheres to the surface of the coke itself, increasing the flammability of the pseudo particles. And the burning speed decreases. Moreover, if the amount of the remaining coke added to the drum mixer 11 exceeds 80% by weight, the amount of coke adhering to the surface of the pseudo particles increases, and the burning speed becomes too high, or the coke inside the pseudo particles is reduced. This is because the amount is insufficient, which impairs the quality of the sinter. in this way,
Actively forming a coke adhesion layer on the surface of the pseudo particles,
By adjusting the adhesion thickness to 100 to 250 μm, as shown in FIG. 4, the productivity of the sintering machine (T / dm
2 ) can be improved to about 29.7 to 33. The pseudo particles exiting the drum mixer 11 are classified by a sieve 22, and the sieve having a size of 10 mm or more is conveyed to a sintering machine and
The size below the sieve is supplied to the drum mixer 11 again as return powder 23.

【0012】[0012]

【実施例】次に、燃焼性に優れた焼結用原料の造粒方法
の実施例について説明する。鉄鉱石粉や返し鉱等からな
る粉鉱石を用い、500μm未満が40重量%と70重
量%含有する粉鉱石に、蛇紋岩や石灰石粉を12重量%
配合して、直径が4m、全長が20mのドラムミキサー
を7回転/分で回転しながら、水6.5重量%を外掛け
で添加し、コークスの全添加量を2.5重量%にしてコ
ークスのドラムミキサー内の添加条件を変えて造粒を行
って、焼結機の焼結鉱の生産性(T/d・m2 )を比較
した。表1に示すように、実施例1では、500μm未
満が40重量%の粉鉱石に、ドラムミキサーの1/2
(0.5L)の位置で、残部80重量%のコークスを添
加したものと、同様に500μm未満が70重量%の粉
鉱石に、ドラムミキサーの1/2(0.5L)の位置
で、残部のコークスを80重量%添加した場合であり、
生産性(T/d・m2 )が35、31であり、いずれも
良好な結果が得られた。実施例2では、500μm未満
が40重量%の粉鉱石に、ドラムミキサーの3/4
(0.75L)の位置で、残部50重量%のコークスを
添加したものと、同様に500μm未満が70重量%の
粉鉱石に、ドラムミキサーの3/4(0.75L)の位
置で、残部50重量%のコークスを添加した場合であ
り、生産性(T/d・m2 )が32、32であり、いず
れも良好な結果が得られた。
EXAMPLES Next, examples of a method for granulating raw materials for sintering having excellent flammability will be described. 12% by weight of serpentine or limestone powder in powder ore containing less than 500 μm of 40% by weight and 70% by weight using iron ore powder or rock ore
While mixing, while rotating a drum mixer having a diameter of 4 m and a total length of 20 m at 7 revolutions / minute, 6.5 wt% of water was externally added to make the total amount of coke added to 2.5 wt%. performing granulation by changing the addition conditions in the coke drum mixer to compare the productivity of sintered ore in the sintering machine (T / d · m 2) . As shown in Table 1, in Example 1, less than 500 μm was added to 40% by weight of fine powder ore by の of a drum mixer.
(0.5 L) at the position where the remaining 80% by weight of coke was added, and similarly, at less than 500 μm, 70% by weight of the fine ore, at a position 1/2 (0.5 L) of the drum mixer, 80% by weight of coke was added,
Productivity (T / d · m 2) is 35, 31, both good results were obtained. In Example 2, 40% by weight ore less than 500 μm was added to 3/4 of the drum mixer.
(0.75 L) at the position where 50% by weight of coke was added, and similarly, at less than 500 μm, 70% by weight of fine ore, at the position of 3/4 (0.75 L) of the drum mixer, a case of adding 50 wt% of the coke productivity (T / d · m 2) is 32, 32, both good results were obtained.

【0013】[0013]

【表1】 [Table 1]

【0014】これに対して、表2に示すように、500
μm未満が40重量%の粉鉱石と、500μm未満が7
0重量%の粉鉱石にそれぞれ全添加量が粉鉱石の2.5
重量%であるコークスを全てドラムミキサーの入口で添
加した場合であり、それぞれの生産性(T/d・m2
が25、20と極めて悪い結果であった。
On the other hand, as shown in Table 2, 500
40% by weight of fine ore with less than μm and 7 with less than 500 μm
0% by weight of each of the fine ores has a total amount of 2.5% of the fine ore.
A case of adding coke is the weight percent at the entrance of all drum mixer, each of productivity (T / d · m 2)
However, the results were extremely bad, 25 and 20.

【0015】[0015]

【表2】 [Table 2]

【0016】以上、本発明の実施の形態を説明したが、
本発明は、上記した形態に限定されるものでなく、要旨
を逸脱しない条件の変更等は全て本発明の適用範囲であ
る。例えば、粉鉱石は、各産地から出荷される銘柄の鉄
鉱石粉等の他に、乾燥スラジ、焼結鉱粉、庫下粉、ペレ
ット用粉等の鉄分を含有するものを一部配合して用いる
ことができる。更に、ドラムミキサーは傾斜角度を調整
して滞留時間の調整や回転数を遅くする等により全長を
短くしたり、長くすることができる。
The embodiments of the present invention have been described above.
The present invention is not limited to the above-described embodiment, and all changes in conditions that do not depart from the gist are within the scope of the present invention. For example, as for fine ore, in addition to iron ore powder of a brand to be shipped from each locality, a dry sludge, a sintered ore powder, an underground powder, a powder containing iron, such as a pellet powder, are partially mixed and used. be able to. Further, the length of the drum mixer can be shortened or lengthened by adjusting the inclination angle to adjust the residence time or the number of revolutions.

【0017】[0017]

【発明の効果】請求項1〜3記載の燃焼性に優れた焼結
用原料の造粒方法は、ドラムミキサーに粉鉱石とコーク
スを添加して攪拌を行って擬似粒子に造粒する焼結用原
料の造粒方法において、予め粉鉱石に全添加量の20〜
50重量%のコークスを添加し、残部のコークスを、ド
ラムミキサーの全長をLとして、装入口から0.5L〜
0.98Lの範囲に添加するので、焼結機内に装入した
擬似粒子の燃焼性や燃焼速度が良くなり適正な燃焼温度
で焼結でき、焼結鉱の生産性や歩留り等が向上できる。
According to the present invention, there is provided a method for granulating raw materials for sintering having excellent flammability, wherein fine ore and coke are added to a drum mixer and agitated to granulate into pseudo particles. In the method of granulating raw materials, the total amount of 20-
50% by weight of coke was added, and the remaining coke was added to the drum mixer at a total length of 0.5 L from the charging inlet.
Since it is added in the range of 0.98 L, the flammability and burning rate of the pseudo particles charged in the sintering machine are improved, and sintering can be performed at an appropriate burning temperature, so that the productivity and yield of sintered ore can be improved.

【0018】特に、請求項2記載の燃焼性に優れた焼結
用原料の造粒方法は、粉鉱石が粒度が500μm未満の
微粉を30〜70重量%含んでいるので、造粒した擬似
粒子の内部や外側にコークスが埋没するのを抑制して、
燃焼性が低下するのを防止し、焼結鉱の生産性をより向
上できる。
In particular, according to the method for granulating a raw material for sintering excellent in flammability according to claim 2, since the fine ore contains 30 to 70% by weight of fine powder having a particle size of less than 500 µm, the granulated pseudo-particles To prevent coke from being buried inside and outside the
A decrease in flammability can be prevented, and the productivity of sinter can be further improved.

【0019】請求項3記載の燃焼性に優れた焼結用原料
の造粒方法は、残部のコークスの添加位置を、500μ
m未満の粉鉱石の含有量に応じて調整するので、擬似粒
子の内部に含まれるコークスと表層に付着するコークス
を適正に調整でき、燃焼性や燃焼速度が良好になり、焼
結鉱の生産性や歩留り等を安定して向上できる。
According to a third aspect of the present invention, there is provided a method for granulating a raw material for sintering having excellent flammability, wherein the remaining coke is added at a position of 500 μm.
m or less, the coke contained inside the pseudo-particles and the coke adhering to the surface layer can be properly adjusted, and the flammability and combustion speed are improved, and the production of sinter ore is improved. Properties and yield can be stably improved.

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

【図1】本発明の一実施の形態に係る燃焼性に優れた焼
結用原料の造粒方法に適用される焼結用原料の造粒装置
の全体図である。
FIG. 1 is an overall view of an apparatus for granulating a sintering raw material applied to a method for granulating a sintering raw material excellent in combustibility according to one embodiment of the present invention.

【図2】同造粒方法に適用する原料の粉鉱石とコークス
の粒径ごとの容積%を比較したグラフである。
FIG. 2 is a graph showing a comparison between volume percentages of fine particles of raw material ore and coke for each particle size applied to the granulation method.

【図3】500μm未満の粉鉱石の重量%とコークス付
着厚を200μmとするコークスの添加位置の関係を示
すグラフである。
FIG. 3 is a graph showing the relationship between the weight percentage of fine ore of less than 500 μm and the coke addition position where the coke adhesion thickness is 200 μm.

【図4】コークス付着厚と焼結機の生産性の関係を示す
グラフである。
FIG. 4 is a graph showing the relationship between the coke adhesion thickness and the productivity of a sintering machine.

【符号の説明】[Explanation of symbols]

10:焼結用原料の造粒装置、11:ドラムミキサー、
12:貯蔵ホッパー、13:フィーダ、14:貯蔵ホッ
パー、15:フィーダ、16:ベルトコンベア、17:
ベルトコンベア、18:ベルトコンベア、19:貯蔵ホ
ッパー、20:フィーダ、21:スプレー配管、22:
篩、23:返し粉
10: Granulator for raw materials for sintering, 11: Drum mixer,
12: Storage hopper, 13: Feeder, 14: Storage hopper, 15: Feeder, 16: Belt conveyor, 17:
Belt conveyor, 18: Belt conveyor, 19: Storage hopper, 20: Feeder, 21: Spray piping, 22:
Sieve, 23: flour

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ドラムミキサーで粉鉱石とコークスを攪
拌して擬似粒子に造粒する焼結用原料の造粒方法におい
て、予め前記コークスの全添加量の20〜50重量%と
前記粉鉱石とを前記ドラムミキサーに装入し、残部のコ
ークスを、前記ドラムミキサーの全長をLとして装入口
から0.5L〜0.98Lの範囲に添加することを特徴
とする燃焼性に優れた焼結用原料の造粒方法。
1. A method for granulating a raw material for sintering in which fine ore and coke are agitated by a drum mixer to form pseudo particles, wherein 20 to 50% by weight of the total amount of the coke and the fine ore are mixed in advance. Is charged into the drum mixer, and the remaining coke is added to the drum mixer in the range of 0.5 L to 0.98 L from the charging inlet with the total length of the drum mixer being L. Granulation method of raw material.
【請求項2】 請求項1記載の燃焼性に優れた焼結用原
料の造粒方法において、前記粉鉱石は、粒度が500μ
m未満の微粉を30〜70重量%含んでいる燃焼性に優
れた焼結用原料の造粒方法。
2. The method of claim 1, wherein the fine ore has a particle size of 500 μm.
A method for granulating a raw material for sintering which contains 30 to 70% by weight of fine powder having a particle size of less than 30 m and has excellent flammability.
【請求項3】 請求項1又は2記載の燃焼性に優れた焼
結用原料の造粒方法において、前記残部のコークスの添
加位置を500μm未満の粉鉱石の含有量に応じて調整
する燃焼性に優れた焼結用原料の造粒方法。
3. The method for granulating a raw material for sintering excellent in flammability according to claim 1 or 2, wherein the addition position of the remaining coke is adjusted according to the content of fine ore less than 500 μm. Excellent method for granulating raw materials for sintering.
JP09777199A 1999-04-05 1999-04-05 Granulation method for raw materials for sintering with excellent flammability Expired - Lifetime JP4087982B2 (en)

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WO2004055224A1 (en) * 2002-12-17 2004-07-01 Jfe Steel Corporation Process for producing sintering feedstock and apparatus therefor
US7402191B2 (en) 2002-12-17 2008-07-22 Jfe Steel Corporation Process for producing sintering feedstock and apparatus therefor
WO2007063603A1 (en) * 2005-12-02 2007-06-07 Kyouzai Kogyo Co., Ltd. Method of granulating sintering raw material and process for producing sintered ore
US7875097B2 (en) 2005-12-02 2011-01-25 Kyouzai Kogyo Co., Ltd. Method of granulating raw material for sintering, and method of manufacturing sintered iron ore
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