JP4317316B2 - Pretreatment method of sintering raw materials - Google Patents

Pretreatment method of sintering raw materials Download PDF

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JP4317316B2
JP4317316B2 JP2000202272A JP2000202272A JP4317316B2 JP 4317316 B2 JP4317316 B2 JP 4317316B2 JP 2000202272 A JP2000202272 A JP 2000202272A JP 2000202272 A JP2000202272 A JP 2000202272A JP 4317316 B2 JP4317316 B2 JP 4317316B2
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iron
powder
containing powder
binder
quicklime
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JP2002020820A (en
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武 今井
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Nippon Steel Corp
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Nippon Steel Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、含鉄粉にバインダーを添加して疑似粒に造粒する焼結原料の事前処理方法に関する。
【0002】
【従来の技術】
従来、焼結原料は、含鉄ダスト、スラジ、鉄鉱石粉等の含鉄粉に、生石灰粉や消石灰等からなるバインダーと、燃料であるコークス粉を添加し、ロータリーキルン式、あるいはパン式等の造粒装置により疑似粒子に加工される。
疑似粒子は、無端状に連結されたパレットに装入され、点火炉で疑似粒子に付着したコークスが点火されて燃焼を開始する。この燃焼は、上層から下層に移動して全層が焼結して焼結鉱が製造される。
しかし、この造粒方法では、図5に示すように、ベルトコンベア51で搬送中の含鉄粉50の上に、貯蔵ホッパ52に貯蔵されたバインダーの一例である生石灰粉53をフィーダ54から切り出して造粒装置に送る。
そして、図6に示すように、造粒装置によって、比較的大きな粒子の含鉄粉50からなる核鉱石55の周囲に、生石灰粉53の粘着性を利用して残りの含鉄粉50が付着し、凝集層56が形成されて疑似粒子57となる。
しかし、核鉱石55の周囲に付着して形成される凝集層56内に、未反応の生石灰粉53が存在し、含鉄粉50の細粒を十分に付着させて凝集層56とすることができない。
その結果、未造粒の含鉄粉50が残り、造粒歩留りの低下、生石灰粉53の増使用によるコストの上昇、疑似粒子57の強度の低下等が生じている。
この対策として、特開平4−254533号公報に記載されているように、生石灰粉を予め水を加えてスラリーにしてベルトコンベアに流し込んでから、このスラリーの上に含鉄粉を切り出して積層して搬送し、造粒装置に供給して疑似粒子を製造することにより、疑似粒子を形成する際に、細粒からの核の形成を促進して造粒を向上させることが行われている。
更に、特公昭59−17171号公報に記載されているように、ベルトコンベアの上に積層した含鉄粉の上に添加された生石灰粉に散水して、事前に生石灰粉を湿潤処理して水和反応を促進させることにより、粘着性を良好にして造粒効率の向上を図ることが行われている。
【0003】
【発明が解決しようとする課題】
しかしながら、特開平4−254533号公報に記載された方法では、水和反応よって生成した消石灰(Ca(OH)2 )を多量に含む粘着性の高いスラリー上に含鉄粉を切り出して積層するため、スラリー中の消石灰を含鉄粉に均一に分散させることができず、造粒過程で疑似粒子に消石灰の濃淡が発生する。
その結果、未造粒の含鉄粉により造粒歩留りが低下し、生石灰粉の使用量の増加によるコストの上昇や疑似粒子の強度の低下等が生じる。
更に、特公昭59−17171号公報に記載された方法では、含鉄粉の上に生石灰粉を積層してから、この生石灰に散水を行って水和反応をさせて消石灰にするので、バインダーとなる消石灰が含鉄粉上で固化したり、消石灰が凝結し易く、含鉄粉内への分散を十分に行うことが困難である。
しかも、造粒装置で疑似粒子にする際に、分散性が悪いことから、疑似粒子の周囲に形成される凝集層に消石灰の凝結部が存在し、特開平4−254533号公報に記載された方法と同様に、未造粒の含鉄粉によって造粒歩留りが低下する。しかも、生石灰の使用量の増加による造粒コストの上昇や疑似粒子の強度の低下等が生じると言った問題がある。
【0004】
本発明はかかる事情に鑑みてなされたもので、含鉄粉の未造粒を抑制して造粒歩留りを高め、生石灰粉等のバインダーの使用量を少なくして造粒効率を向上し、造粒コストの低減や疑似粒子の品質を向上できる焼結原料の事前処理方法を提供することを目的とする。
【0005】
【課題を解決するための手段】
前記目的に沿う本発明の焼結原料の事前処理方法は、含鉄粉にバインダーを添加して前記含鉄粉を造粒する焼結原料の事前処理方法において、前記バインダーに生石灰粉を用い、前記含鉄粉に水を添加してから1分以内に、前記生石灰粉を固気比が100以下になるように、気体に混合して前記含鉄粉に吹き付け、前記生石灰粉を分散して前記含鉄粉に添加する。
なお、分散とは、バインダーをベルトコンベア等から落下させて添加する際に、落下流を散らす外力を付与するか、あるいは予め気体や水にバインダーを混合して添加することを言う。
この方法により、バインダーを含鉄粉中に均一に分布させることができ、核鉱石の周囲に、バインダーの粘着作用を利用して含鉄粉を効率良く付着させることができ、良好な凝集層を形成して造粒効率を向上することができる。
【0006】
ここで、前記バインダーに生石灰粉を用いる。
これにより、良好な分散性と粘着性を発現でき、含鉄粉の造粒をより促進することができ、疑似粒子の強度等の品質を高めることができる。
【0007】
更に、前記バインダーを気体に混合して吹き付ける。
バインダーを気体の吹き付け力により分散するので、含鉄粉に含まれる水分を吸着してバインダーが凝結するのを防止でき、含鉄粉の疑似粒子化に有効に利用することができる。
【0008】
また、前記バインダーの固気比を100以下にする。
含鉄粉に添加する際のバインダーの固気比(気体の重さに対する固体の重さの割合)を所定の範囲にしているので、バインダーの分散性が大幅に向上し、含鉄粉等の水分とバインダーの反応による凝結を安定して抑制できる。
【0009】
【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。
本発明者等は、含鉄粉を造粒して疑似粒子を製造する際に、バインダーの添加量を増加しても十分な疑似粒子化が図れないことがあることに着目し、この現象について鋭意研究を行った。
そして、造粒性の悪かった疑似粒子について調査したところ、核鉱石の周囲に付着した含鉄粉の一部に凝結したバインダーが散見され、十分にバインダーとしての働きが行われておらず、しかも、その原因が、バインダーが含鉄粉の水分等を吸着して凝結を起し、如何に造粒装置で混練を強化しても含鉄粉内のバインダーの凝結を改善することができず、結果として造粒効率が低下していることが分かった。
そこで、バインダーを分散させて含鉄粉に添加することにより、バインダーの凝結が抑制され、含鉄粉の粘着を効率良く行い得ることを知見し、本発明の完成に至った。
ここで、図1は本発明の一実施の形態に係る焼結原料の事前処理方法に適用される造粒装置の全体図、図2は同造粒装置のA−A矢視断面図、図3は空気量と固気比の関係を表すグラフ、図4は生石灰反応率と焼結鉱の生産量の関係を表すグラフである。
図1及び図2に示すように、本発明の一実施の形態に係る焼結原料の事前処理方法に用いられる造粒装置10は、円筒状のロータリーキルン12と、鉄鉱石粉、スラジ、集塵ダスト等からなる含鉄粉11をロータリーキルン12内に切り出すシュート13と、ロータリーキルン12の回転により内部で転動する含鉄粉11にバインダーの一例である生石灰粉14を空気と共に圧送して吹き付ける生石灰粉供給管15と、含鉄粉11が造粒されて形成された疑似粒子を搬送するベルトコンベア16を備えている。
【0010】
次に、造粒装置10を用いて本実施の形態に係る焼結原料の事前処理方法について説明する。
含鉄粉11をシュート13からロータリーキルン12内に10〜15トン/分切り出し、ロータリーキルン12を3〜9回/分で回転させて、水をロータリーキルン12の含鉄粉11に0.1〜2重量%添加し、含鉄粉11を転動させながら矢印(図1)の方向に含鉄粉11を移動させる。
転動の開始から1.0〜2.0分以内に水を添加することにより、比較的大きいサイズの含鉄粉11が核鉱石となり、その周囲に含鉄粉11の細粒が付着して疑似粒子を形成し始める。
水の添加と同時、あるいは水の添加から1.0分以内に、生石灰粉供給管15から空気と混合した生石灰粉14を搬送し、含鉄粉11の表面に吹き付ける。
生石灰粉14は、転動している含鉄粉11の表面に連続して散布される。
ここで、転動開始から2分以上経て水を添加したり、また、生石灰粉の添加が水の添加から1分以上を過ぎて行われると、ロータリーキルン内での造粒時間が不足して十分な造粒が困難になる。
そして、生石灰粉14は、含鉄粉11が転動しているため、常に新たな含鉄粉11の表面に散布でき、空気が混入された生石灰粉14の散布と含鉄粉11の転動の相乗作用により、極めて均一に含鉄粉11内に生石灰粉14を混合することができる。
含鉄粉11に混合された生石灰粉14は、含鉄粉11中の水分や添加した水と下式の反応により粘着性の良好な消石灰(Ca(OH)2 )を生成する。
CaO+H2 O→Ca(OH)2
この消石灰は、図2に示すように、ロータリーキルン12の回転によって含鉄粉11が転動することにより、前述の核鉱石を起点にして、その周囲に細粒の含鉄粉11を粘着させ、良好な凝集層を形成でき、未造粒の粉の少ない品質の優れた疑似粒子を形成することができる。
【0011】
生石灰粉を空気に混合した場合の固気比は、図3に示すように、生石灰粉の搬送量が5〜20t/hrの場合、搬送に用いる空気量が200Nm3 未満になると急激に上昇する。
固気比が100を超えると、搬送中に脈動等が生じて生石灰粉の搬送量が大きく変動するため、含鉄粉に分布する生石灰粉が不均一になり、水和反応した際に生石灰粉が残存する。
その結果、残存した生石灰粉の粘着作用が悪いため、核鉱石の周囲に含鉄粉の細粒を粘着させることができず、造粒効率が大幅に悪くなり、疑似粒子の強度も低下する。
従って、生石灰粉14の添加量あるいは搬送用の空気量を調整し、固気比を100以下になるよう搬送気体量や吹き付ける固体量を調整する。
ここで、固気比は、添加生石灰粉の重量を搬送空気重量で除した値である。
【0012】
また、生石灰粉の分布状態の良否及び造粒効率の良否を簡易的に把握する方法として、疑似粒子を分析して、未反応の生石灰粉の量と水分と反応して生成した消石灰の量を測定することで判別することができる。
即ち、疑似粒子に含まれる未反応の生石灰粉の量と水分と反応して生成した消石灰量をそれぞれ測定し、添加生石灰粉量に対する消石灰の比率を求め、この比率(生石灰反応率)を60〜80%に高く維持することにより、造粒効率を向上することができ、未造粒の粉に発生も防止することができる。
このようにして製造された疑似粒子は、生石灰粉の水和反応による消石灰が均一に分布しているため、造粒された疑似粒子の強度等の品質が良好であり、これを焼結機に供給して焼結鉱が製造され、製造された焼結鉱の品質も向上することができる。
【0013】
【実施例】
次に、本発明に係る焼結原料の事前処理方法の実施例について説明する。
鉄鉱石粉と集塵ダストを混合した含鉄粉を13トン/分シュートからロータリーキルン内に切り出し、ロータリーキルンを6.5回/分の速さで回転させ、含鉄粉に1.0重量%の水を添加した。
そして、水を添加してから1分を経過した時点で、生石灰粉供給管から空気と生石灰粉の固気比を10となるように調整して転動する含鉄粉に吹き付けて造粒を行い、生石灰反応率と焼結鉱の生産性を調査した。
その結果、図4に示すように、固気比を10にして生石灰粉の吹き付けた本発明では、生石灰反応率が60〜80%の範囲に向上でき、造粒した疑似粒子を用いて焼結を行ったところ、焼結鉱の生産量が630〜640t/hrと大幅に向上することができた。
これに対し、ベルトコンベアで搬送中の含鉄粉の上に、分散することなく単に生石灰粉をフィーダーから切り出す従来の添加の場合では、生石灰粉の分散性が悪く、含鉄粉内に均一に分布させることができないため、疑似粒子の断面を調査した結果、生石灰粉の未反応の塊が散見され、生石灰反応率が40〜60%未満と低位(通常)になっている。
その結果、疑似粒子の生成が悪くなり、未造粒の含鉄粉が発生し、この疑似粒子を用いて焼結を行った際の焼結鉱の生産量も最大で620t/hr未満と大幅に低下した。
【0014】
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。
例えばバインダーを添加する位置は、ベルトコンベア上の含鉄粉にバインダーを搬送用の空気に混合して吹き付けたり、フィーダ等から落下しているバインダーに空気を吹き付ける等の外力を付与することにより、分散して添加するか、あるいはベルトコンベア上での添加と造粒装置内での添加に分けたいわゆる分割添加を行うこともできる
【0015】
【発明の効果】
請求項記載の焼結原料の事前処理方法においては、バインダーを分散して含鉄粉に添加するので、バインダーの使用量を少なくして造粒歩留りを向上することができ、造粒コストを低減することができる。しかも、疑似粒子の強度を改善することができ、焼結鉱の生産性や品質を向上することができる。
【0016】
請求項記載の焼結原料の事前処理方法においては、バインダーに生石灰粉を用いるので、良好な分散性と粘着性を発現でき、造粒効率をより向上することができる。
【0017】
請求項記載の焼結原料の事前処理方法においては、バインダーを気体に混合して吹き付けるので、バインダーの凝結を防止して造粒効率を高め、疑似粒子の品質を安定して向上することができる。
【0018】
請求項記載の焼結原料の事前処理方法においては、バインダーの固気比を100以下にしているので、バインダーをより均一に添加することができ、造粒効率の大幅な向上とバインダーの使用量の節減が可能になる。
【図面の簡単な説明】
【図1】本発明の一実施の形態に係る焼結原料の事前処理方法に適用される造粒装置の全体図である。
【図2】同造粒装置のA−A矢視断面図である。
【図3】空気量と固気比の関係を表すグラフである。
【図4】生石灰反応率と焼結鉱の生産量の関係を表すグラフである。
【図5】従来用いられている焼結原料の造粒装置の全体図である。
【図6】従来の造粒装置で製造された疑似粒子の断面の模式図である。
【符号の説明】
10:造粒装置、11:含鉄粉、12:ロータリーキルン、13:シュート、14:生石灰粉、15:生石灰粉供給管、16:ベルトコンベア
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for pre-processing a sintered raw material in which a binder is added to iron-containing powder and granulated into pseudo grains.
[0002]
[Prior art]
Conventionally, sintering raw materials are iron-containing powders such as iron-containing dust, sludge, iron ore powder, etc. Add a binder made of quick lime powder or slaked lime and coke powder as fuel, and granulators such as rotary kiln type or bread type Is processed into pseudo particles.
The pseudo particles are charged into an endlessly connected pallet, and coke attached to the pseudo particles is ignited in an ignition furnace to start combustion. This combustion moves from the upper layer to the lower layer, and all layers are sintered to produce a sintered ore.
However, in this granulation method, as shown in FIG. 5, quick lime powder 53, which is an example of a binder stored in the storage hopper 52, is cut out from the feeder 54 on the iron-containing powder 50 being conveyed by the belt conveyor 51. Send to granulator.
And as shown in FIG. 6, the remaining iron-containing powder 50 adheres to the circumference | surroundings of the nuclear ore 55 which consists of the iron-containing powder 50 of a comparatively big particle | grain using the adhesiveness of the quicklime powder 53, as shown in FIG. Aggregated layer 56 is formed to become pseudo particles 57.
However, the unreacted quicklime powder 53 exists in the agglomerated layer 56 formed by adhering to the periphery of the nuclear ore 55, and the fine particles of the iron-containing powder 50 cannot be sufficiently adhered to form the agglomerated layer 56. .
As a result, the ungranulated iron-containing powder 50 remains, resulting in a decrease in granulation yield, an increase in cost due to the increased use of quick lime powder 53, a decrease in strength of the pseudo particles 57, and the like.
As a countermeasure, as described in JP-A-4-254533, quick lime powder is preliminarily added with water to form a slurry and poured into a belt conveyor, and iron-containing powder is cut out and laminated on the slurry. When forming pseudo | simulated particles by conveying and supplying to a granulating apparatus and manufacturing pseudo | simulated particles, formation of the nucleus from a fine grain is accelerated | stimulated and granulation is performed.
Furthermore, as described in Japanese Examined Patent Publication No. 59-17171, water is added to the quicklime powder added on the iron-containing powder laminated on the belt conveyor, and the quicklime powder is wet-treated and hydrated in advance. By promoting the reaction, the tackiness is improved to improve the granulation efficiency.
[0003]
[Problems to be solved by the invention]
However, in the method described in JP-A-4-254533, the iron-containing powder is cut out and laminated on a highly sticky slurry containing a large amount of slaked lime (Ca (OH) 2 ) generated by a hydration reaction. The slaked lime in the slurry cannot be uniformly dispersed in the iron-containing powder, and the density of slaked lime is generated in the pseudo particles during the granulation process.
As a result, the granulation yield decreases due to the non-granulated iron-containing powder, resulting in an increase in cost and a decrease in the strength of the pseudo particles due to an increase in the amount of quicklime powder used.
Furthermore, in the method described in Japanese Examined Patent Publication No. 59-17171, quick lime powder is laminated on iron-containing powder, and then the quick lime is sprinkled to make a hydration reaction to obtain slaked lime, which becomes a binder. Slaked lime is solidified on the iron-containing powder or slaked lime is likely to condense, and it is difficult to sufficiently disperse it in the iron-containing powder.
Moreover, since the dispersibility is poor when the pseudo particles are formed by the granulating apparatus, there is a condensed portion of slaked lime in the aggregated layer formed around the pseudo particles, which is described in JP-A-4-254533. Similar to the method, the granulation yield is reduced by the ungranulated iron-containing powder. In addition, there is a problem that an increase in granulation cost due to an increase in the amount of quicklime used and a decrease in the strength of pseudo particles occur.
[0004]
The present invention has been made in view of such circumstances, to improve the granulation yield by suppressing the ungranulated iron-containing powder, improve the granulation efficiency by reducing the amount of binder such as quick lime powder, granulation It aims at providing the pre-processing method of the sintering raw material which can reduce the cost and improve the quality of pseudo particles.
[0005]
[Means for Solving the Problems]
Preprocessing method for sintering the raw material of the present invention along the object, in the pre-processing method of the sintering raw material to granulate the ferrous powder by adding a binder to the iron-containing powder, with lime powder to the binder, the ferrous Within 1 minute after adding water to the powder, the quicklime powder is mixed with gas and sprayed onto the iron-containing powder so that the solid-gas ratio is 100 or less, and the quicklime powder is dispersed to the iron-containing powder. Added.
In addition, dispersion | distribution means giving the external force which scatters a falling flow, or mixing and adding a binder to gas or water previously, when dropping and adding a binder from a belt conveyor.
By this method, the binder can be uniformly distributed in the iron-containing powder, and the iron-containing powder can be efficiently attached around the core ore by using the adhesive action of the binder, thereby forming a good aggregated layer. The granulation efficiency can be improved.
[0006]
Here, Ru with lime powder to the binder.
Thereby, favorable dispersibility and adhesiveness can be expressed, granulation of iron-containing powder can be further promoted, and quality such as strength of pseudo particles can be enhanced.
[0007]
Furthermore, Ru spraying a mixture of the binder into a gas.
Since the binder is dispersed by the blowing force of the gas, it is possible to prevent the binder from condensing by adsorbing moisture contained in the iron-containing powder, and can be effectively used for making the iron-containing powder pseudo particles.
[0008]
Also, you a solid-gas ratio of the binder to 100 below.
Since the solid-gas ratio of the binder when added to the iron-containing powder (the ratio of the weight of the solid to the weight of the gas) is within a predetermined range, the dispersibility of the binder is greatly improved, and the moisture content of the iron-containing powder and the like Aggregation due to the reaction of the binder can be stably suppressed.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.
The inventors of the present invention have paid attention to this phenomenon, paying attention to the fact that, when producing pseudo particles by granulating iron-containing powder, sufficient pseudo particles may not be achieved even if the amount of binder added is increased. I did research.
And when we investigated the pseudo particles with poor granulation properties, some of the iron-containing powder adhered to the periphery of the nuclear ore was found to be coagulated, and it did not function as a binder sufficiently. The cause of this is that the binder adsorbs moisture etc. of the iron-containing powder and causes the setting, and no matter how the kneading is strengthened by the granulator, the setting of the binder in the iron-containing powder cannot be improved. It was found that the grain efficiency was reduced.
Thus, it has been found that by adding the binder to the iron-containing powder by dispersing the binder, the coagulation of the binder can be suppressed and the iron-containing powder can be effectively adhered, and the present invention has been completed.
Here, FIG. 1 is an overall view of a granulating apparatus applied to a sintering raw material pretreatment method according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along the line AA of the granulating apparatus. 3 is a graph showing the relationship between the amount of air and the solid-gas ratio, and FIG. 4 is a graph showing the relationship between the quicklime reaction rate and the production amount of sintered ore.
As shown in FIG.1 and FIG.2, the granulation apparatus 10 used for the pre-processing method of the sintering raw material which concerns on one embodiment of this invention is a cylindrical rotary kiln 12, iron ore powder, sludge, dust collection dust. An iron-containing powder 11 made of, for example, a chute 13 for cutting the iron-containing powder 11 into the rotary kiln 12, and a quick-lime powder supply pipe 15 that presses and sprays quick-lime powder 14, which is an example of a binder, together with air to the iron-containing powder 11 that rolls inside the rotary kiln 12. And a belt conveyor 16 that conveys pseudo particles formed by granulating the iron-containing powder 11.
[0010]
Next, the pretreatment method of the sintering raw material which concerns on this Embodiment using the granulator 10 is demonstrated.
The iron-containing powder 11 is cut from the chute 13 into the rotary kiln 12 at 10 to 15 tons / min, the rotary kiln 12 is rotated at 3 to 9 times / min, and water is added to the iron-containing powder 11 of the rotary kiln 12 at 0.1 to 2% by weight. Then, the iron-containing powder 11 is moved in the direction of the arrow (FIG. 1) while rolling the iron-containing powder 11.
By adding water within 1.0 to 2.0 minutes from the start of rolling, the iron-containing powder 11 having a relatively large size becomes a nuclear ore, and the fine particles of the iron-containing powder 11 adhere to the surroundings and become pseudo particles. Begin to form.
Simultaneously with the addition of water or within 1.0 minute from the addition of water, the quicklime powder 14 mixed with air is conveyed from the quicklime powder supply pipe 15 and sprayed onto the surface of the iron-containing powder 11.
The quicklime powder 14 is continuously sprayed on the surface of the iron-containing powder 11 that is rolling.
Here, if water is added after 2 minutes or more from the start of rolling, or if quick lime powder is added after 1 minute or more from the addition of water, the granulation time in the rotary kiln is insufficient and sufficient. Granulation becomes difficult.
And since the iron-containing powder 11 is rolling, the quick lime powder 14 can always be sprinkled on the surface of the new iron-containing powder 11, and the synergistic action of spraying the quick-lime powder 14 mixed with air and rolling of the iron-containing powder 11 is possible. Thereby, the quicklime powder 14 can be mixed in the iron-containing powder 11 very uniformly.
The quick lime powder 14 mixed with the iron-containing powder 11 generates slaked lime (Ca (OH) 2 ) with good adhesiveness by the reaction of the water in the iron-containing powder 11 or the added water with the following formula.
CaO + H 2 O → Ca (OH) 2
As shown in FIG. 2, the slaked lime is formed by causing the iron-containing powder 11 to roll by the rotation of the rotary kiln 12, thereby sticking the fine iron-containing powder 11 around the above-mentioned nuclear ore, An agglomerated layer can be formed, and excellent quality pseudo-particles with less ungranulated powder can be formed.
[0011]
As shown in FIG. 3, the solid-gas ratio when quicklime powder is mixed with air rapidly increases when the amount of quicklime powder transported is 5 to 20 t / hr and the amount of air used for transport is less than 200 Nm 3. .
If the solid-gas ratio exceeds 100, pulsation and the like occur during transportation, and the transport amount of quick lime powder fluctuates greatly. Remains.
As a result, since the sticking action of the remaining quicklime powder is poor, the fine particles of the iron-containing powder cannot be stuck around the nuclear ore, the granulation efficiency is greatly deteriorated, and the strength of the pseudo particles is also reduced.
Therefore, the amount of quick lime powder 14 added or the amount of air for conveyance is adjusted, and the amount of carrier gas and the amount of solid to be sprayed are adjusted so that the solid-gas ratio becomes 100 or less.
Here, the solid-gas ratio is a value obtained by dividing the weight of the added quicklime powder by the carrier air weight.
[0012]
In addition, as a method for easily grasping the quality of the distribution of quicklime powder and the quality of granulation efficiency, the pseudo particles are analyzed, and the amount of unreacted quicklime powder and the amount of slaked lime generated by reacting with moisture are calculated. It can be determined by measuring.
That is, the amount of unreacted quicklime powder contained in the pseudo particles and the amount of slaked lime generated by reacting with moisture are respectively measured, the ratio of slaked lime to the amount of added quicklime powder is determined, and this ratio (quicklime reaction rate) is set to 60 to By keeping it high at 80%, the granulation efficiency can be improved, and the occurrence of ungranulated powder can also be prevented.
Since the pseudo particles produced in this way have a uniform distribution of slaked lime due to the hydration reaction of quicklime powder, the quality of the granulated pseudo particles is good, and this is used as a sintering machine. The sinter is produced by supplying, and the quality of the produced sinter can be improved.
[0013]
【Example】
Next, the Example of the pre-processing method of the sintering raw material which concerns on this invention is described.
Cut iron-containing powder mixed with iron ore powder and dust-collecting dust into a rotary kiln from a 13-ton / min chute, rotate the rotary kiln at a speed of 6.5 times / min, and add 1.0% by weight of water to the iron-containing powder. did.
And when 1 minute has passed since water was added, granulation is carried out by spraying on the iron-containing powder rolling by adjusting the solid-gas ratio of air and quicklime powder to 10 from the quicklime powder supply pipe. Then, the quicklime reaction rate and the productivity of sintered ore were investigated.
As a result, as shown in FIG. 4, in the present invention in which quick-lime powder is sprayed with a solid-gas ratio of 10, the quick-lime reaction rate can be improved to a range of 60 to 80%, and sintering is performed using granulated pseudo particles. As a result, the production of sintered ore was significantly improved to 630 to 640 t / hr.
On the other hand, in the case of conventional addition in which quick lime powder is simply cut out from the feeder without being dispersed on the iron-containing powder being conveyed by the belt conveyor, the dispersibility of the quick lime powder is poor and is uniformly distributed in the iron-containing powder. Therefore, as a result of investigating the cross section of the pseudo particles, unreacted lumps of quicklime powder are scattered, and the quicklime reaction rate is as low as 40 to 60% (normal).
As a result, the generation of pseudo particles is deteriorated, ungranulated iron-containing powder is generated, and the production of sintered ore when sintering using these pseudo particles is significantly less than 620 t / hr at maximum. Declined.
[0014]
Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and all changes in conditions and the like that do not depart from the gist are within the scope of the present invention.
For example , the position where the binder is added can be obtained by mixing the iron-containing powder on the belt conveyor with the binder mixed with air for transportation, or by applying an external force such as blowing air onto the binder falling from a feeder or the like. It is also possible to add in a dispersed manner, or to perform so-called divided addition divided into addition on the belt conveyor and addition in the granulator .
[0015]
【The invention's effect】
In the sintering material pretreatment method according to claim 1 , since the binder is dispersed and added to the iron-containing powder, the amount of the binder used can be reduced to improve the granulation yield, and the granulation cost can be reduced. can do. Moreover, the strength of the pseudo particles can be improved, and the productivity and quality of the sintered ore can be improved.
[0016]
In the pretreatment method of the sintered raw material according to claim 1 , since quick lime powder is used for the binder, good dispersibility and adhesiveness can be expressed, and the granulation efficiency can be further improved.
[0017]
In the pretreatment method of the sintered raw material according to claim 1 , since the binder is mixed with the gas and sprayed, the aggregation of the binder can be prevented to increase the granulation efficiency, and the quality of the pseudo particles can be stably improved. it can.
[0018]
In the pretreatment method of the sintering raw material according to claim 1 , since the solid-gas ratio of the binder is 100 or less, the binder can be added more uniformly, greatly improving the granulation efficiency and using the binder. Savings in volume are possible.
[Brief description of the drawings]
FIG. 1 is an overall view of a granulating apparatus applied to a sintering raw material pretreatment method according to an embodiment of the present invention.
FIG. 2 is a cross-sectional view of the granulator taken along the line AA.
FIG. 3 is a graph showing the relationship between the air amount and the solid-gas ratio.
FIG. 4 is a graph showing the relationship between quicklime reaction rate and the production of sintered ore.
FIG. 5 is an overall view of a conventional granulating apparatus for a sintering raw material.
FIG. 6 is a schematic view of a cross section of a pseudo particle produced by a conventional granulator.
[Explanation of symbols]
10: Granulator, 11: Iron-containing powder, 12: Rotary kiln, 13: Chute, 14: Quicklime powder, 15: Quicklime powder supply pipe, 16: Belt conveyor

Claims (1)

含鉄粉にバインダーを添加して前記含鉄粉を造粒する焼結原料の事前処理方法において、前記バインダーに生石灰粉を用い、前記含鉄粉に水を添加してから1分以内に、前記生石灰粉を固気比が100以下になるように、気体に混合して前記含鉄粉に吹き付け、前記生石灰粉を分散して前記含鉄粉に添加することを特徴とする焼結原料の事前処理方法。In the pre-processing method of the sintering raw material which granulates the iron-containing powder by adding a binder to the iron-containing powder, the quick lime powder is used within 1 minute after adding quick lime powder to the binder and adding water to the iron-containing powder. Is mixed with gas so that the solid-gas ratio is 100 or less, sprayed onto the iron-containing powder, and the quicklime powder is dispersed and added to the iron-containing powder.
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