JPS6075527A - Treatment of dust generated in an ironworks - Google Patents

Treatment of dust generated in an ironworks

Info

Publication number
JPS6075527A
JPS6075527A JP58183899A JP18389983A JPS6075527A JP S6075527 A JPS6075527 A JP S6075527A JP 58183899 A JP58183899 A JP 58183899A JP 18389983 A JP18389983 A JP 18389983A JP S6075527 A JPS6075527 A JP S6075527A
Authority
JP
Japan
Prior art keywords
powder
dust
water content
collected
iron
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
JP58183899A
Other languages
Japanese (ja)
Other versions
JPS6248734B2 (en
Inventor
Yoshimasa Suga
須賀 芳睿
Kunio Hachisuga
蜂須賀 邦夫
Toru Wakabayashi
徹 若林
Hiroyoshi Uchida
内田 博祥
Noburo Ayabe
綾部 信郎
Masakazu Yamaguchi
政和 山口
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.)
Yoshikawa Kogyo Co Ltd
Nippon Steel Corp
Original Assignee
Yoshikawa Kogyo Co Ltd
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 Yoshikawa Kogyo Co Ltd, Nippon Steel Corp filed Critical Yoshikawa Kogyo Co Ltd
Priority to JP58183899A priority Critical patent/JPS6075527A/en
Publication of JPS6075527A publication Critical patent/JPS6075527A/en
Publication of JPS6248734B2 publication Critical patent/JPS6248734B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

PURPOSE:To reutilize dust contg. iron and caustic lime powder generated in an ironworks as materials for producing iron by treating them rationally depending on wet condition and chemical property of the dust at the collected stage. CONSTITUTION:Collected dust contg. iron and lime is classified to wet collected dust consisting primarily of fine powder and ore and lime powder consisting of coarse particle. The ore and lime powder are crushed in dry atmosphere with blown air to produce crushed product contg. >=65% particles having <=45mu particle size and <=5% water. On one hand, the wet collected dust is dehydrated to <=40% water content, or it is blended after dehydration with separately collected fine powder of low water content to adjust the water content of the blended product to <=40%. When it is further blended with above-described crushed caustic lime powder and spread on a drying floor, temp. is elevated by the heat of reaction and contained water is evaporated to reduce the water content to <=25%. The dried powder is blended with the above described crushed ore powder together with binder and kneaded to reduce the water content to <=10%, then granulated by rolling and utilized for the source of iron.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は製鉄工場で発生する石灰粉及び含鉄粉塵を、
捕集の形式及び捕築時の粒度によって分別処理を行い、
これら処理物を配合・造粒し、再度鉄鋼製造に利用し得
るよう造粒処理する製鉄工場で発生する製鉄粉塵の処理
方法に関する。
[Detailed Description of the Invention] [Industrial Field of Application] This invention is a method for removing lime powder and iron-containing dust generated in a steel factory.
Sorting is done according to the type of collection and particle size at the time of collection,
The present invention relates to a method for treating iron-making dust generated in a steel-making factory, in which these processed materials are blended and granulated, and granulated so that they can be reused in steel manufacturing.

〔従来技術〕[Prior art]

一般に製鉄工場では、その製造工程において多くの種類
の粉塵が発生ずる。これらの発生粉塵は鉱石粉、焼結粉
、製鋼粉、圧延スケール、生石灰粉或は直接還元炉粉等
多くの種類があり、これらが鉄鋼製造の工程に応じて多
岐にわたり発生する。
In general, many types of dust are generated in steel factories during the manufacturing process. There are many types of these generated dusts, such as ore powder, sintered powder, steelmaking powder, rolling scale, quicklime powder, and direct reduction furnace powder, and these are generated in a wide variety of ways depending on the steel manufacturing process.

これら発生粉塵は環境汚染防止及び一部は再資源化のた
めに乾式或は湿式捕集され、そのあるものは再利用に供
するための処理方法が提案されている。
These generated dusts are collected by dry or wet methods to prevent environmental pollution and some of them are recycled, and treatment methods have been proposed for some of them to be reused.

例えば湿式捕集された転炉型鋼における転炉スラグや圧
延工程から捕集される圧延スラリ等の湿潤含鉄微細粉の
乾燥方法として、本発明者等は天日による省エネルギ乾
燥方法を開発し、特願昭55−136431号として出
願し、更にはこれら含鉄微細粉の有効な造粒方法を開発
し、特願昭55−136430号を出願した。又この他
製鉄工場において発生する含油、含鉄スラリを利用した
M鋼用ペレットの製造方法が特公昭57−43622号
公報に発表されている。しかし、これら公知の製鉄粉塵
の処理においては、単一種の含鉄粉塵或は似かよった性
状の粉塵を単−的に処理する方法を提供するに止まり、
製鉄工場内で発生する再資源化可能な粉塵を、その性状
によりたくみに組合せ、利用する総合的な粉塵処理方法
に想到するに及んでいない。
For example, as a method for drying wet iron-containing fine powder such as converter slag in wet-collected converter-type steel or rolling slurry collected from the rolling process, the present inventors have developed an energy-saving drying method using the sun. This patent application was filed as Japanese Patent Application No. 136431/1980, and an effective granulation method for these iron-containing fine powders was developed and Japanese Patent Application No. 136430/1982 was filed. In addition, Japanese Patent Publication No. 57-43622 discloses a method for producing pellets for M steel using oil-containing and iron-containing slurry generated in steel factories. However, these known methods for treating iron dust only provide a method for simply treating a single type of iron-containing dust or dust with similar properties;
A comprehensive dust treatment method that utilizes the recyclable dust generated in steel factories by skillfully combining them according to their properties has not yet been devised.

〔発明の目的〕[Purpose of the invention]

本発明は溶鉱炉形式の製鉄工場或は直接還元製鉄形式の
製鉄工場たるを問わず、製鉄工場内で発生する含鉄粉塵
及び生石灰粉を、その捕集時の湿潤状態及び化学性状を
合理的に活用して総合的に処理することによって鉄源と
して再利用に供し得る、安価にして、かつ優れた製鉄用
ペレットの省エネルギー製造方法を提供することを目的
になさ3− れたものである。
The present invention rationally utilizes the wet state and chemical properties of iron-containing dust and quicklime powder generated in a steel factory, regardless of whether it is a blast furnace type steel factory or a direct reduction type steel factory. The purpose of this invention is to provide an energy-saving method for manufacturing pellets for iron making, which can be reused as an iron source by comprehensively processing the pellets at low cost, and which is excellent.

〔発明の構成〕[Structure of the invention]

以下、本発明について詳細に述べる。 The present invention will be described in detail below.

鉄鋼製造工程においては、高炉ガス灰、焼結粉。In the steel manufacturing process, blast furnace gas ash and sintered powder.

転炉ダスト、電気炉ダスト、圧延スケール、鉱石粉が、
直接還元製鉄においては還元鉄粉が発生し、或は副原料
用の石灰焼成においては生石灰粉等多くの種類の粉塵が
発生ずる。
Converter dust, electric furnace dust, rolling scale, ore powder,
In direct reduction iron making, reduced iron powder is generated, and in calcining lime for use as an auxiliary raw material, many types of dust such as quicklime powder are generated.

これらの粉塵はサイクロン、或はベンチュリ等積々の捕
集装置によって捕集され、それらは捕集の手段或は捕集
の場所によって第1表に例示した様に種々の性状9粒度
を有する。
These dusts are collected by a collection of collection devices such as cyclones or venturis, and have various properties and particle sizes as illustrated in Table 1 depending on the means of collection or location of collection.

4− 第1表から明らかなように製鉄工場で発生ずる各種粉塵
はその発生酸は捕集の場所によって粒度が異なり、例え
ば鉱石粉は溶鉱炉対応処理工程或は直接還元鉄工場にお
ける還元装置対応の処理工程で発生し、連鋳スケールは
溶鋼の連鋳工程で発生する。鉱石粉又は微粉鉄源の造粒
工程で発生ずる造粒ブラケットの篩分は粉、或は連鋳ス
ケール等は比較的多くの粗粒粉を含有する。又これら粗
粒粉を多く含む発生粉の水分の含有量は比較的少ない。
4- As is clear from Table 1, the particle size of the various types of dust generated in steel factories differs depending on the place where they are collected. For example, ore powder is treated in a blast furnace treatment process or directly reduced in a reduction equipment factory. Continuous casting scale is generated during the continuous casting process of molten steel. The sieve of the granulation bracket generated in the granulation process of ore powder or fine powder iron source contains powder, or the continuous casting scale, etc., contains a relatively large amount of coarse powder. Further, the water content of the generated powder containing a large amount of coarse powder is relatively low.

又、製鉄工場において鉄鉱石と共に鉄鋼製造の原料とし
て欠かすことのできない生石灰製造時或はそのハンドリ
ング時に発生ずる生石灰粉は水分の含有が無く、比較的
粗粒粉が多い。
In addition, quicklime powder generated during the production or handling of quicklime, which is indispensable as a raw material for steel production along with iron ore in a steel factory, does not contain moisture and is relatively coarse-grained.

一方、製鋼粉塵、或は還元鉄製造工場における還元炉発
生粉塵等は粒度が微細であり、その捕集が湿式であるた
めに、これを再利用処理に好適な水分量例えば10%と
いったような低水分量に脱水するには極めて困難であり
、多大なエネルギコストを必要とする。
On the other hand, steelmaking dust or dust generated from reduction furnaces in reduced iron manufacturing plants have fine particles and are collected using a wet method, so they are collected at a moisture content of 10%, which is suitable for reuse. Dehydration to a low water content is extremely difficult and requires a large amount of energy cost.

本発明者等は上記の如く鉄鋼製造において、発生の場所
、或は捕集の方法を異にする粉粒物を粒度構成、含有水
分量及び性質によって区分し、類似するものを集合し、
これらを適宜に組合せ、処理することによって、製鉄発
生粉粒物を総合的に処理し、鉄源として再利用する方法
について種々に研究を重ね、本発明を完成するに至った
As mentioned above, in steel manufacturing, the present inventors classify powder and granules that differ in their generation location or collection method according to their particle size structure, moisture content, and properties, and collect similar materials,
By appropriately combining and processing these methods, we have conducted various studies on a method for comprehensively processing powder and granules generated in iron manufacturing and reusing them as an iron source, leading to the completion of the present invention.

即ち、本発明は製鉄工場において捕集した含鉄粉塵及び
石灰粉塵を微細粉粒を主体とする湿式捕集粉塵と粗粒粉
の多い捕集粉とに区分し、湿式捕集した微細粉粒は、フ
ィルタープレス等により1次的な脱水を行う。一方、水
分含有量が比較的少なく且つ乾燥し易い粗粒粉は送風乾
燥雰囲気中において粒度45μm以下の微細粒が65%
以上となるように粉砕し、これら粉砕物中、生石灰粉は
前記脱水微細粉粒と配合し、必要に応じて別に準備せる
生石灰粉を加えて混合して、これを乾燥床に展開し、粉
粒の含有水分と配合生石灰との反応熱により混合粉粒体
を昇温させ、これを逐次耕耘展開して乾燥させて後、前
記した鉱石粉等の低水分の乾燥粉砕粉及びセメント等の
バインダとを配合して転動造粒することを特徴とする。
That is, the present invention classifies iron-containing dust and lime dust collected in a steel factory into wet-collected dust mainly consisting of fine particles and collected powder containing many coarse particles. , perform primary dehydration using a filter press, etc. On the other hand, coarse powder with a relatively low water content and easy to dry contains 65% fine particles with a particle size of 45 μm or less in an air drying atmosphere.
The quicklime powder is mixed with the dehydrated fine powder particles, and if necessary, quicklime powder prepared separately is added and mixed. This is spread on a drying bed and powdered. The temperature of the mixed granular material is raised by the heat of reaction between the moisture content of the grains and the blended quicklime, and after this is successively cultivated and dried, it is mixed with the above-mentioned low-moisture dry pulverized powder such as ore powder and a binder such as cement. It is characterized by blending and tumbling granulation.

製鉄においては、原料鉄鉱石の事前処理例えば溶鉱炉へ
装入される鉄鉱石の粒度調整、粉鉱石等の焼結、或は鉄
鉱石の直接還元における原料鉱石の整粒工程で発生ずる
鉱石粉粒はそのままベレットに転勤造粒するには比較的
大粒が多く粉砕しなければならない。しかもこれらの比
較的粗粒を含む発生粉は共通して捕集時の水分含有量が
少なく且つ熱風或は冷風による送風乾燥性も良好である
In steelmaking, ore powder particles are generated during pre-processing of raw material iron ore, such as particle size adjustment of iron ore charged into a blast furnace, sintering of fine ore, or sizing process of raw material ore during direct reduction of iron ore. In order to directly transfer to pellets for granulation, many relatively large particles must be crushed. Moreover, these generated powders containing relatively coarse particles commonly have a low moisture content when collected and have good drying properties when blown with hot or cold air.

本発明はこのような比較的粗粒を含み粉砕を必要とする
乾燥が容易な低含水捕集粉を第1グループに区分し、こ
れを熱風或は冷風の送気装置を有するロータリミル等の
粉砕装置にて送気しながら粉砕処理を行ない、45μm
以下の粒度粉が65%以上になるように微粉砕する。4
5μm以下の粒度の微粉が65%以下になると、転勤造
粒において造粒効率が劣化し、且つ良質の造粒物を得ら
れない。
The present invention classifies such low water content collection powder that contains relatively coarse particles and requires pulverization and is easy to dry into the first group, and processes it using a rotary mill or the like having a hot air or cold air blowing device. Grinding is performed using a grinding device while blowing air, and the size is 45 μm.
Pulverize so that the following particle size powder is 65% or more. 4
If the proportion of fine powder with a particle size of 5 μm or less is 65% or less, the granulation efficiency deteriorates in transfer granulation, and high-quality granules cannot be obtained.

又、」二記粉砕においては水分は5%以下とすることが
必要で、粉砕物中の水分が5%以上になる8− と粉砕効率が低下する。本発明の上記粉砕において送風
気流中での粉砕について例示したが、これに限るもので
はなく、予め乾燥を行い、この乾燥物を粉砕することも
できる。
Furthermore, in the pulverization described in item 2, the moisture content must be kept at 5% or less, and if the moisture content in the pulverized product exceeds 5%, the pulverization efficiency decreases. In the above-mentioned pulverization of the present invention, pulverization in a blown air stream is exemplified, but the invention is not limited to this, and it is also possible to dry the material in advance and pulverize the dried product.

又、本発明においては副原料である生石灰の製造過程或
は処理過程で捕集される生石灰も−に記第1グループに
区分されるが、比較的粗粒粉を含む生石灰粉は水分を含
まず、乾燥なしに粉砕処理を行うことができる。
In addition, in the present invention, quicklime collected during the production or treatment process of quicklime, which is an auxiliary raw material, is also classified into the first group described in -, but quicklime powder containing relatively coarse powder contains water. The pulverization process can be carried out without drying.

一方、転炉スラリ、或は鉄鉱石還元炉スラリ等の如き集
塵スラリは混式捕集されるために含有水分が極めて高く
、しかも脱水乾燥の極めて困難な粉砕の必要のない微細
粉は第2グループに区分される。これら第2グループ内
の水分含有量の大なる微細粉粒はフィルタープレス等適
当な脱水手段により含有水分量が50%以下に脱水する
。この脱水は、その脱水粉粒が別に捕集された低含水含
鉄微細粉粒物と配合されて耕耘乾燥される場合は10%
以上であってもよいが、上記低含水粉粒物を配合しない
時は40%以下に脱水すべきである。本発9− 明において耕耘乾燥される微細粉の水分含有量は40%
以下にされるが、これが40%以上になると耕耘乾燥床
に展開される粉粒層表面に浸出水層が形成され、乾燥が
著しく阻害される。父上記脱水において含有水分量が5
0%以上では、耕耘乾燥前に水分調整のために配合され
る前記低含水の含鉄微細粉の必要量が多くなり、工場内
捕集粉では不足することになる。
On the other hand, dust collection slurries such as converter slurry or iron ore reduction furnace slurry contain extremely high moisture content because they are collected in a mixed manner. It is divided into two groups. These fine particles in the second group with a high water content are dehydrated to a water content of 50% or less by a suitable dehydrating means such as a filter press. This dehydration is 10% when the dehydrated powder is mixed with separately collected low water content iron-containing fine powder and tilled and dried.
The water content may be higher than that, but when the above-mentioned low water content powder is not blended, the water content should be dehydrated to 40% or less. Present invention 9- Moisture content of fine powder tilled and dried in Ming is 40%
However, if it exceeds 40%, a leachate layer will be formed on the surface of the powder layer spread on the tilling and drying bed, and drying will be significantly inhibited. The water content in the above dehydration is 5
If it is 0% or more, the required amount of the low water content iron-containing fine powder that is blended for moisture adjustment before tilling and drying becomes large, and the powder collected in the factory will not be enough.

上記脱水処理された微細粉粒は前記第1グループの生石
灰粉をその水分量に応じて添加され、これが含水微細粉
粒内において適宜の分布が得られるように混合され、コ
ンクリート張り等の耕耘乾燥床に層状に展開される。
Quicklime powder of the first group is added to the dehydrated fine powder according to its moisture content, and this is mixed so as to obtain an appropriate distribution within the water-containing fine powder, and then tilled and dried for concrete laying, etc. It is spread out in layers on the floor.

耕耘乾燥床における展開層の厚さは特に限定されること
はないが、耕耘鋤起し能力、或は水分の蒸散能力等によ
り適宜に選ぶことができ、50cm以下の厚みとするの
が好ましい乾燥結果を得ることができる。
The thickness of the spread layer in the tillage drying bed is not particularly limited, but can be selected appropriately depending on the tillage ability, water evaporation ability, etc., and the thickness is preferably 50 cm or less. You can get results.

耕耘床に展開される混合微細粉粒は配合生石灰と含有水
分との次の反応により発熱し微細粉粒を昇温する。
The mixed fine powder spread on the till bed generates heat due to the following reaction between the blended quicklime and the water content, raising the temperature of the fine powder.

CaO+ H20=Ca (OH) 2 + 1.50
00kcal/ mo1本発明者等は集塵スラリ類(水
分30〜50%)にその含有水分の化学当量の生石灰粉
を配合した時の層状展開物の温度上昇は夏、冬を通じて
40℃前後の大巾な上昇を得ることができた。
CaO+ H20=Ca(OH)2+1.50
00 kcal/mo1 The present inventors have found that when lime powder is added to dust collection slurry (30 to 50% moisture) in a chemical equivalent of the water content, the temperature rise of the layered product is around 40℃ throughout summer and winter. I was able to get a huge increase.

上記反応により温度上昇を得た層状展開粉粒物は、耕耘
機等の如き適当な鋤起し攪拌手段により鋤起しされ、攪
拌混合することによって充分に反応し、温度上昇した高
温粒面を大気中に曝露せしめると共に、天日により、或
は更に必要に応じて熱風等により補充的に加熱され乾燥
が促進される。
The layered spread powder grains whose temperature has increased due to the above reaction are plowed by a suitable plowing and stirring means such as a tiller, and by stirring and mixing, they are sufficiently reacted and the high-temperature grain surfaces whose temperature has been raised are plowed. While exposing to the atmosphere, drying is accelerated by supplementary heating by the sun or, if necessary, by hot air.

本発明において反応昇温のために配合した石灰分は、更
に鉄鋼精錬時の造滓剤として有効に利用される。
In the present invention, the lime content added for raising the reaction temperature is further effectively used as a slag forming agent during steel refining.

上記の如(して耕耘乾燥された微細粉粒は水分含有量が
25%以下にされるが、この水分含有量が25%以上で
は前記第1グループの粉砕微細粉粒の配合によってもそ
の混合物の水分含有量を造粒に好適な水分量とすること
ができない。水分含有量が25%以下に乾燥された上記
第2グループの乾燥微細粉粒は、前記した第1グループ
の乾燥粉砕粉粒に配合されるが、この配合においては、
第1グループの低含水粉粒は第2グループの乾燥粉の水
分含有量に応じて配合され、例えば第2グループの乾燥
粉の水分含有量が高い場合には、第1グループの低含水
粉砕粉を多くして混合物の平均水分含有量が10%以下
になるようにする。
The moisture content of the tilled and dried fine powder as described above is reduced to 25% or less, but if the moisture content is 25% or more, the blend of the pulverized fine powder of the first group may also cause the mixture to have a moisture content of 25% or less. It is not possible to make the water content suitable for granulation.The dry fine powder particles of the second group, which have been dried to a moisture content of 25% or less, are the same as the dry pulverized powder particles of the first group. However, in this formulation,
The low water content powder of the first group is blended according to the water content of the dry powder of the second group. For example, when the water content of the dry powder of the second group is high, the low water content ground powder of the first group is mixed. is increased so that the average water content of the mixture is 10% or less.

かくて水分含有量が10%以下になるように配合し、混
合した微細粉粒は更にセメント等のバインダを添加して
充分に混合し、更にポーリングドラム、或はポーリング
ディスク等の転勤造粒装置に装入して転勤造粒する。こ
の造粒物は更に養生され必要な強度となす。本発明の製
鉄工場において発生する製鉄粉塵の処理は、上記した如
く、発生粉塵をその粒度、含有水分によって第1グルー
プ及び第2グループに区分し、これを総合的観点に基づ
いてなされるものであって、低湿類相粉の乾燥、粉砕及
び湿潤微粒粉への生石灰粉の効果的活用による乾燥処理
についでこれら夫々のグループ12− の処理微細粉粒はその水分含有量に応じて適宜に配合さ
れ、転勤造粒に適した水分量に調整することを大きな特
徴とするものである。
In this way, the water content is blended to be 10% or less, and the mixed fine powder is further added with a binder such as cement and mixed thoroughly, and then processed using a transfer granulation device such as a polling drum or a polling disc. The granules are transferred to the granulator and granulated. This granulated material is further cured to obtain the necessary strength. As mentioned above, the treatment of the iron dust generated in the steel factory of the present invention is carried out based on the comprehensive viewpoint of classifying the generated dust into the first group and the second group according to its particle size and moisture content. Then, after drying and pulverizing the low-humidity phase powder and effectively utilizing quicklime powder to the wet fine powder, each of these treated fine powders of Group 12- is appropriately blended according to their moisture content. The major feature is that the moisture content can be adjusted to be suitable for transfer granulation.

〔実施例〕〔Example〕

本発明の実施例について以下更に述べる。 Examples of the present invention will be further described below.

製鉄工場で発生した第2表に示す捕集粉粒物をその粒度
構成により第1グループと第2グループとに区分し、第
1グループに属する比較的粗粒物の多い粉粒物を温度7
oo℃の熱気流中のローラミルにて粉砕し、第3表に示
す微細粉粒を得た。
The collected powder and granules shown in Table 2 generated at a steel factory are divided into the first group and the second group according to their particle size composition, and the powder and granules belonging to the first group, which have a relatively large amount of coarse particles, are heated to a temperature of 7.
It was pulverized in a roller mill in a hot air stream at oo°C to obtain the fine powder shown in Table 3.

=13− 一方、第2グループに区分された水分含有量の多い集塵
スラリと石灰マッドはフィルタープレスにより脱水し、
含有水分を50%となし、これを第1グループの生石灰
の粉砕粉粒と配合し、更に第2グループの水分含有量の
少ない電炉スラリと混合した。この混合物の水分含有量
は32%であった。
=13- On the other hand, the dust slurry and lime mud with high water content classified into the second group were dehydrated using a filter press.
The moisture content was set to 50%, and this was blended with the crushed quicklime powder of the first group, and further mixed with the electric furnace slurry with a low moisture content of the second group. The moisture content of this mixture was 32%.

この混合物を充分に攪拌して配合生石灰を均一に分布さ
せ、コンクリート張りの乾燥床に39 cmの厚さに層
状に展開し、これを24時間静置して微細粉粒中の水分
と配合生石灰とを充分反応させて微細粉粒を昇温させた
。ついで、これを耕耘機を用いて耕耘攪拌しながら天日
乾燥下において水分の蒸発放散を行った。耕耘攪拌を1
時間間隔で繰り返し、水分を23%に低下させた後、こ
れに前記第1グループの乾燥粉砕微細粉粒の鉱石粉及び
ベレット篩下粉を配合して、混合物の水分含有量を8%
に調整した。
This mixture was sufficiently stirred to evenly distribute the mixed quicklime, spread out in a layer of 39 cm thick on a concrete drying bed, and left to stand for 24 hours until the moisture in the fine powder and the mixed quicklime were mixed. The temperature of the fine powder was raised by sufficiently reacting with the powder. Then, the water was evaporated and dissipated under the sun while being tilled and agitated using a tiller. 1 tilling and stirring
Repeatedly at time intervals, after reducing the moisture content to 23%, the first group of dry ground fine powder ore powder and pellet undersieve powder were added to this to reduce the moisture content of the mixture to 8%.
Adjusted to.

ついで上記混合物にバインダとしてセメントを8%添加
混合すると共に水分を10%に調整してディスク型造粒
機にて転勤造粒し、3日間養生し、−15= 圧壊強度60 kg /ベレット、粒Pi!5〜10鶴
の粒を95%の収率で得ることができた。
Next, 8% cement was added as a binder to the above mixture, the moisture content was adjusted to 10%, and the mixture was granulated using a disk-type granulator, and cured for 3 days to obtain -15 = crushing strength of 60 kg/bellet, granules. Pi! It was possible to obtain grains of 5 to 10 grains with a yield of 95%.

この養生粒は焼結機或は直接還元炉への装入物として好
適であり、又製鋼用温度調整材として有効に使用され得
るものである。
This cured grain is suitable as a charge to a sintering machine or a direct reduction furnace, and can also be effectively used as a temperature regulating material for steel manufacturing.

〔発明の効果〕〔Effect of the invention〕

本発明は上記の如くであるので製鉄工場で発生する有価
粉塵を少ないエネルギーでもって最も合理的に且つ効率
的に再利用に好適な粒状物に形成することのできる有用
な製鉄粉塵の回収処理方法である。
As described above, the present invention is a useful method for recovering and processing iron-making dust that can most rationally and efficiently form valuable dust generated in iron-making factories into granular materials suitable for reuse with less energy. It is.

特許出願人 新日本製鐵株式會社(ばか1名)代理人 
手掘 益(ほか2名) 16−
Patent applicant Nippon Steel Corporation (one idiot) agent
Masu Tebori (and 2 others) 16-

Claims (1)

【特許請求の範囲】[Claims] 1、捕集した含鉄粉塵及び石灰粉塵を、微細粉分を主体
とする湿式捕集粉塵と粗粒分の多し)鉱石粉及び石灰粉
とに区分し、上記鉱石粉及び石灰粉は送風乾燥雰囲気に
おいて粉砕して、粒度45μm以下が65%以上、水分
を5%以下となし、一方、前記湿式捕集した微細粉は脱
水して水分含有量40%以下とするかあるいは脱水後さ
らに別に捕集した低含水微細粉と配合して水分含有量を
40%以下となし、上記粉砕生石灰と配合し、乾燥床に
展開し、前記配合石灰と前記微細粉の含有水との反応熱
により昇温させ、適宜これを耕耘展開して含有水を蒸散
乾燥して含有水分を6%以下となし、ついでこれを前記
粉砕鉱石粉にバインダーと共に配合混練し、水分を10
%以下に凋湿し転勤造粒することを特徴とする製鉄工場
で発生ずる製鉄粉塵の処理方法。
1. The collected iron-containing dust and lime dust are divided into wet-collected dust mainly consisting of fine particles and ore powder and lime powder (with a large proportion of coarse particles), and the ore powder and lime powder are air-dried. The fine powder collected by the wet method is either dehydrated to have a moisture content of 40% or less, or is further captured separately after dehydration. The mixture is mixed with the collected low water content fine powder to make the moisture content 40% or less, mixed with the above-mentioned crushed quicklime, spread on a drying bed, and heated by the heat of reaction between the mixed lime and the water contained in the fine powder. The water content is reduced to 6% or less by cultivating and drying it to remove water contained in it.Then, this is mixed and kneaded with the crushed ore powder together with a binder to reduce the water content by 10%.
A method for treating ironmaking dust generated in a steelmaking factory, which is characterized by dampening the dust to less than % and granulating it by transfer.
JP58183899A 1983-09-30 1983-09-30 Treatment of dust generated in an ironworks Granted JPS6075527A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58183899A JPS6075527A (en) 1983-09-30 1983-09-30 Treatment of dust generated in an ironworks

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58183899A JPS6075527A (en) 1983-09-30 1983-09-30 Treatment of dust generated in an ironworks

Publications (2)

Publication Number Publication Date
JPS6075527A true JPS6075527A (en) 1985-04-27
JPS6248734B2 JPS6248734B2 (en) 1987-10-15

Family

ID=16143756

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58183899A Granted JPS6075527A (en) 1983-09-30 1983-09-30 Treatment of dust generated in an ironworks

Country Status (1)

Country Link
JP (1) JPS6075527A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1004681A1 (en) * 1998-11-24 2000-05-31 Kabushiki Kaisha Kobe Seiko Sho Pellets incorporated with carbonaceous material and method of producing reduced iron
JP2003247027A (en) * 2002-02-25 2003-09-05 Nippon Steel Corp METHOD OF TREATING Cr-CONTAINING SLUDGE AND INCINERATION RESIDUAL DROSS OR THE LIKE AND PELLET FOR STEEL MAKING OBTAINED THEREBY

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1004681A1 (en) * 1998-11-24 2000-05-31 Kabushiki Kaisha Kobe Seiko Sho Pellets incorporated with carbonaceous material and method of producing reduced iron
JP2003247027A (en) * 2002-02-25 2003-09-05 Nippon Steel Corp METHOD OF TREATING Cr-CONTAINING SLUDGE AND INCINERATION RESIDUAL DROSS OR THE LIKE AND PELLET FOR STEEL MAKING OBTAINED THEREBY

Also Published As

Publication number Publication date
JPS6248734B2 (en) 1987-10-15

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