JPS6199638A - Manufacture of iron powder from pig iron-containing slag - Google Patents

Manufacture of iron powder from pig iron-containing slag

Info

Publication number
JPS6199638A
JPS6199638A JP59222448A JP22244884A JPS6199638A JP S6199638 A JPS6199638 A JP S6199638A JP 59222448 A JP59222448 A JP 59222448A JP 22244884 A JP22244884 A JP 22244884A JP S6199638 A JPS6199638 A JP S6199638A
Authority
JP
Japan
Prior art keywords
iron
iron powder
particle size
slag
pig
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.)
Pending
Application number
JP59222448A
Other languages
Japanese (ja)
Inventor
Isao Sato
勇夫 佐藤
Mikio Harada
幹雄 原田
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 Jiryoku Senko Co Ltd
Original Assignee
Nippon Jiryoku Senko 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 Nippon Jiryoku Senko Co Ltd filed Critical Nippon Jiryoku Senko Co Ltd
Priority to JP59222448A priority Critical patent/JPS6199638A/en
Publication of JPS6199638A publication Critical patent/JPS6199638A/en
Pending 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

Landscapes

  • Furnace Details (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To obtain the iron powder for a concrete reinforcing aggregate, a chemical body warmer, or the like, by refining the metallic iron content of a pig iron-contg. slag until the iron content gives >=90%, and subjecting the refined metallic iron content to screening, particle size regulation, or the like, to gain the stabilization of properties. CONSTITUTION:The pig iron-contg. slag is subjected to crush and magnetic separation, required times, repeatedly, to be recovered by separation, and is refined until the metallic iron content gives >=90% in total. The refined matter is subjected either to screening and grain size regulation or to pulverization and air classification. In this way, pulverized iron of each particle size having uniform and stable quality can be obtained.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は製鉄所で発生する含銑鉄スラグから回収した金
属鉄分を原料として、常温下で破砕、空気分綾、磁選等
の物理的!!鉱千手段加えることによりコンクリート強
化骨材用、化学カイロ用、脱酸素剤用等の鉄粉を製造す
る方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention uses metallic iron recovered from pig iron-containing slag generated at a steelworks as a raw material, and uses physical methods such as crushing, air mixing, and magnetic separation at room temperature. ! This invention relates to a method for producing iron powder for use in concrete reinforcement aggregates, chemical body warmers, oxygen scavengers, etc. by adding minerals to the iron powder.

〔従来の技術〕[Conventional technology]

近年工業用鉄粉は溶接用、化学カイロ用、脱酸素剤用、
コンクリート強化骨材用等の用途が拡大し、製法の開発
研究も多種試みられているが、現在主な製法としては還
元法、アトマイズ法等が挙げられる。その製法をみると
、還元法では高品位の鉄鉱石又はミルスケールと還元剤
を配合し所定温度の還元反応で海U鉄をつくった後、粉
砕、磁選を行ない、必要によっては鉄粉の反応性を高め
るために保水処理を行なっている。アトマイズ法では鋼
の溶湯を高圧水か不活性ガスで噴霧状にして鉄の小粒を
得、更に粉砕性を容易にしかつ脱炭を行なうために焼鈍
し処理を施している。
In recent years, industrial iron powder has been used for welding, chemical warmers, oxygen absorbers,
Its use as concrete reinforcement aggregate has expanded, and various research and development efforts have been made on manufacturing methods, but the main manufacturing methods currently include the reduction method and the atomization method. Looking at its production method, in the reduction method, high-grade iron ore or mill scale and a reducing agent are mixed together and a reduction reaction is performed at a predetermined temperature to produce sea iron, followed by crushing, magnetic separation, and if necessary, reaction of iron powder. Water retention treatment is carried out to improve performance. In the atomization method, molten steel is atomized with high-pressure water or inert gas to obtain small iron particles, which are then annealed to facilitate crushing and decarburization.

〔発明が解決しようとrる問題点〕[Problems that the invention attempts to solve]

上記の製法はどうらも工程が複雑でありまた高品位の原
料が要求され、コスト高となる問題を負っている。本発
明の出願者は製鉄所から発生するスラグ類を原料にして
破砕、粉砕1分級9m分け。
The above-mentioned manufacturing methods have the problem that the steps are complicated and high-quality raw materials are required, resulting in high costs. The applicant of the present invention uses slag generated from steelworks as a raw material to crush and crush into 9 meter classes.

磁力選別を組合せて処理し製鋼用及びセメント製造用鉄
源、道路路盤材等の製造を行なってきたものであるが、
W植した技術と経験により、上述のスラグ処理系の産物
を原料として冶金的或は化学的処理を含まない物理的選
鉱の方法で鉄粉を製造ことについて研究しその方法を見
出した。
It has been used in combination with magnetic sorting to produce iron sources for steel and cement production, road base materials, etc.
Using our technology and experience, we have researched and found a method for producing iron powder by a physical beneficiation method that does not involve metallurgical or chemical treatment using the products of the slag treatment system mentioned above as raw materials.

〔問題を解決するための手段〕[Means to solve the problem]

前述の製造法は、在来のスラグ処理系統から産出された
全鉄分量80%前後の磁着物である金属鉄分を常温下で
の破砕と磁選等の物理選鉱によって、当該磁着物が鉄粉
としての作用を発揮するに足る品位に達するまで夾雑物
のスラグを取り除く精選工程と、tf1選産物を鉄粉の
用途に応じて篩分けし粒度調整するか、微粉砕し空気分
級する工程とからなっている。また用途によっては粒度
vR′!i後の鉄粉に防錆処理を付加する。
The above-mentioned manufacturing method involves crushing metallic iron, which is a magnetic material with a total iron content of around 80% produced from a conventional slag processing system, at room temperature and physical beneficiation such as magnetic separation, to convert the magnetic material into iron powder. It consists of a selection process to remove slag contaminants until it reaches a quality sufficient to exert its function, and a process to sieve and adjust the particle size of the tf1 selected product depending on the purpose of the iron powder, or to finely crush and air classify it. ing. Also, depending on the application, the particle size is vR'! Add rust prevention treatment to the iron powder after i.

〔作 用〕[For production]

本発明の方法の前段の精選工程においては原料の金属鉄
分は磁力選鉱機で磁選したのち磁着物だけを高速衝撃破
砕機にかける。ここでは磁着物粒子中に介在するスラグ
が衝撃で破壊され剥離する。
In the first selection step of the method of the present invention, the metallic iron component of the raw material is magnetically separated using a magnetic separator, and then only the magnetic material is subjected to a high-speed impact crusher. Here, the slag interposed in the magnetic particles is destroyed by the impact and peeled off.

t      粉砕ざ0たスラ′を含む被破砕物は全量
が再び元の磁力選鉱機で磁選されてスラグが除去される
t The entire amount of the crushed material containing the crushed slag' is magnetically separated again in the original magnetic separator to remove the slag.

この磁選と高速[撃破砕は通常電気回路によって、所定
の全鉄品位の精選産物が得られるよう一定回数循環する
回路がセットされている。
This magnetic separation and high-speed crushing are usually carried out by an electric circuit that cycles through the process a certain number of times to obtain a selected product with a predetermined total iron grade.

少段の工程は精選産物を粉砕及び粒度tlJ整等して用
途別に鉄粉をWtJ整する過程にわかれる。即ちコンク
リート強化骨材用には篩分けと粒度調整が行なわれ、化
学カイ1]用及び脱酸素剤用では微粉砕と空気分級が行
なわれる。
The small steps are divided into pulverizing the selected product, adjusting the particle size tlJ, and adjusting the iron powder WtJ according to the purpose. That is, sieving and particle size adjustment are performed for concrete reinforcement aggregate, and fine pulverization and air classification are performed for chemical use and oxygen scavenger use.

一定@以上の酸化能力を必要条件とする化学カイU及び
脱酸素剤用1の鉄粉については、能力を左右する因子は
全鉄品位の他、粒度と比表面積が重要な要素を占めるこ
とが知見されている。本発明の方法では空気分級を伴な
ったボール又はロッドミルによる微粉砕でバラツキの少
ない安定した品質の微粉末鉄粉を任意の粒度ごとに能率
よく取り出すことが可能である。
Regarding iron powders for Chemical Kai U and Oxygen Absorber 1, which require an oxidizing ability of a certain level or higher, the factors that influence the ability are not only the total iron grade, but also the particle size and specific surface area. It has been discovered. In the method of the present invention, fine powder iron powder of stable quality with little variation can be efficiently extracted at any particle size by fine pulverization using a ball or rod mill accompanied by air classification.

〔実施例〕〔Example〕

第1図に示す製造工程に基づいて本発明の実施例につい
て説明する。
Examples of the present invention will be described based on the manufacturing process shown in FIG.

原料粒鉄(別の処理系統で得た含銑鉄スラグの&!選産
物)は鉄粉の最大粒径の1.2m+*lIf!で篩上を
カットして別系統に返し、篩下を磁選して非磁着物はセ
メント製造用鉄源とし、磁着物を高速衝撃破砕機にかけ
た。磁選と高速衝撃破砕の過程では精選産物の全鉄分量
が92%以上となるよう10回の循環破砕を行なったが
その結果は次の通りである。
Raw material granulated iron (&! selected product of pig iron-containing slag obtained in another processing system) has a maximum particle size of 1.2 m + *lIf! The upper part of the sieve was cut and returned to another system, the lower part of the sieve was subjected to magnetic separation, the non-magnetic material was used as a source of iron for cement production, and the magnetic material was passed through a high-speed impact crusher. In the process of magnetic separation and high-speed impact crushing, cyclic crushing was performed 10 times so that the total iron content of the selected product was 92% or more, and the results are as follows.

第1表 原料と精選産物の化学分析値(重量%)第2表
 原料と精選産物の粒度分布(重量%)精選産物は品位
検定後用途別に鉄粉の調整工程へと進む。コンクリート
強化骨材用鉄粉の製造においては、2段III(篩目上
段0.6a+w+、下段0.3i+m)で篩分けて篩上
サイズと中間サイズの産物を一定の割合で混合し、!耳
に使用時までの防錆のために気化性水i3′液型防錆剤
を塗布して鋳圧め処理する。
Table 1: Chemical analysis values of raw materials and selected products (weight %) Table 2: Particle size distribution of raw materials and selected products (weight %) After quality inspection, the selected products proceed to the process of preparing iron powder according to their use. In the production of iron powder for concrete reinforcement aggregate, it is sieved in two stages III (upper sieve size 0.6a+w+, lower sieve size 0.3i+m), and the products of size above the sieve and intermediate size are mixed at a constant ratio. A vaporizable water i3' liquid type rust preventive agent is applied to the ear to prevent rust until use, and the mold is pressed.

銑鉄粒を破砕する場合、組織中に含まれる遊離のカーボ
ン、所謂キッシュグラファイトが析出して鉄粉の調整過
程や製品の使用時に支障を生じるが、本発明の方法によ
る前段の高速衝撃破砕ではスラグ分のみが衝撃破壊され
て#JH1するためグラファイトの発生が少なく清浄な
製品がえられる。粒度調整の2段篩で一定粒度(0,3
mm)以下を除外するのは、−0,15mm粒度の含有
率が高い鉄粉ではコンクリートの早強現象を生じ養生管
理が困難となるためである。
When crushing pig iron grains, free carbon contained in the structure, so-called quiche graphite, precipitates and causes problems during the iron powder preparation process and product use.However, in the first stage of high-speed impact crushing by the method of the present invention, slag Because only the fraction is impact-destructed to #JH1, a clean product with less graphite generation can be obtained. Constant particle size (0,3
The reason why iron powder with a high content of −0.15 mm particle size is excluded is that iron powder with a high content of −0.15 mm particle size causes early strength phenomenon of concrete and makes curing management difficult.

化学カイロ用及び脱酸素剤用鉄粉は精選産物を空気分級
機構を伴なったボールミルに供給して得た。なお、前述
した2段篩で篩分けられた下段篩下産物(−0,3+u
+)も上記のボールミルに供給されることもある。本実
施例における微粉砕方式の概要は第2図の通りで、粉砕
条件は 使用ボールミル    3490avLX 2540m
mφ媒体         45mmφボール13を回
転数        21rpi 給重量        it/ch 空気分級風量     30m”/win、50m’/
winで、結果は次の通りである。
Iron powder for chemical body warmers and oxygen scavengers was obtained by feeding the selected products to a ball mill equipped with an air classification mechanism. In addition, the lower sieve product (−0,3+u
+) may also be supplied to the above ball mill. The outline of the fine pulverization method in this example is shown in Figure 2, and the pulverization conditions are the ball mill used: 3490avLX 2540m
mφ medium 45mmφ ball 13 rotation speed 21rpi Feed weight it/ch Air classification air volume 30m”/win, 50m’/
In win, the result is as follows.

第3表 収 量 注、ミル排鉱口から集塵装置に至る微 細鉄粉の送流ダクトの途中において、 Aは前捕集槽、Bはサイクロン、Cは 集u機のバッグフィルターでそれぞれ 捕集されたもの。Table 3 Yield Note: The fine particles from the mill outlet to the dust collector In the middle of the fine iron powder flow duct, A is the front collection tank, B is the cyclone, and C is the Each with bag filter of collection machine what was collected.

第4表 粒度分布(重量%) 注、サンプルは第3表のAB合計物(以下同じ)第5表
 粒度別全鉄分量41%) 又、集塵機のバッグフィルターで捕集したものの化学分
析値は第6表の通りである。
Table 4: Particle size distribution (wt%) Note: Samples are AB total in Table 3 (the same applies hereinafter) Table 5: Total iron content by particle size: 41%) Also, the chemical analysis value of the sample collected by the bag filter of the dust collector is As shown in Table 6.

第6表 化学成分(重量%) 以上の性状の鉄粉について化学カイロ用鉄粉としての発
熱性及び脱酸素剤用鉄粉としての脱酸素能力を測定した
結果は次の通りであった。
Table 6 Chemical Composition (% by Weight) The results of measuring the heat generation properties of iron powder for chemical body warmers and the oxygen scavenging ability as iron powder for oxygen scavengers for iron powders having the above properties are as follows.

第7表 発熱性試験(東京都条令の方法による。)注、
上の表は保水剤としてヒル石又は木粉を混合調整したも
の。P鉄粉とは、本発明と同−精選物を振動ミルによっ
て微粉砕して得た鉄粉。
Table 7: Pyrogenicity test (according to the Tokyo Metropolitan Ordinance method) Note:
The table above shows a mixture of vermiculite or wood powder as a water retention agent. P iron powder is iron powder obtained by finely pulverizing the same selected material as in the present invention using a vibration mill.

第8表 脱酸素能力試験(残存酸素濃度%)注、同一条
件でvR整した供試体をガスバリヤ−の袋に密封し、5
00 mlの空気を送入して経時酸素濃度を測定した。
Table 8 Oxygen scavenging ability test (residual oxygen concentration %) Note: The specimen subjected to vR preparation under the same conditions was sealed in a gas barrier bag, and
00 ml of air was introduced and the oxygen concentration over time was measured.

第・7表及び第8表における発熱と脱酸の共通の基礎能
力である鉄粉の酸化力については、T−Feの品位は高
くても例えば0.044■膳以下のサイズを1    
  カットした場合は初期酸化力が低いことを実験的に
得ているし、このことは第5表及び第7表についても明
らかである。前述の風量30m3/win、 50m’
/+in及びP鉄粉のp度と全鉄分量のバラツキを解明
した結果は第9表、第10表及び第11表の通りで、P
鉄粉に較べ粒度のバラツキが少なく粒度構成が適切でか
つ非常に安定しており、他社鉄粉に較べ優れた酸化力を
もつ鉄粉であることがわかる。
Regarding the oxidizing power of iron powder, which is the common basic ability of heat generation and deoxidization in Tables 7 and 8, even if the grade of T-Fe is high, for example, if the size is 0.044cm or less,
It has been experimentally found that the initial oxidizing power is low when cut, and this is also clear from Tables 5 and 7. Air volume as mentioned above: 30m3/win, 50m'
The results of elucidating the variation in p degree and total iron content of /+in and P iron powder are shown in Tables 9, 10, and 11.
Compared to iron powder, this iron powder has less variation in particle size, has an appropriate particle size structure, is very stable, and has superior oxidizing power compared to other iron powders.

第9表 製品粒度のバラツキ 第10表 製品粒度のバラツキ割合 上記実胞例にみるように空気分級を伴なう微粉砕におい
ては、収率」く微粒鉄粉を製造することが可能でありし
か6送風Iを変えることによって任、この粒度のものを
1’:Jることかできる。
Table 9: Dispersion of product particle size Table 10: Dispersion ratio of product particle size As shown in the above sample, in fine pulverization accompanied by air classification, it is possible to produce fine iron powder with a high yield. 6 By changing the air blower I, this particle size can be reduced to 1':J.

〔発明の効果〕〔Effect of the invention〕

以上詳細に説明したように本発明の方法によれば、含銑
鉄スラグから得た金属鉄分を原料として冶金的、化学的
処理を全く用いず、常温下での物理選鉱の手段で安価に
、しかも安定した性能をもつカイロ用、脱酸素剤用及び
コンクリート強化骨材用の鉄粉を製造することができる
As explained in detail above, according to the method of the present invention, metallic iron obtained from pig iron-containing slag is used as a raw material, without using any metallurgical or chemical treatment, and at low cost and by means of physical beneficiation at room temperature. It is possible to produce iron powder for use in body warmers, oxygen absorbers, and concrete reinforcement aggregates with stable performance.

なお、本発明の方法の処理系統から副生する産物は第1
図に示すように、製鉄層の鉄源やセメント工場向けの鉄
源として友好利用されるものであり、また閉回路粉砕で
集塵機に捕集きれる産物(第3表及び第6表の産物C)
にはグラファイトが濃縮した形で含まれておりグラファ
イト回収原料となるものである。
Incidentally, the by-product from the treatment system of the method of the present invention is the first
As shown in the figure, it is used as an iron source for steel manufacturing layers and cement factories, and it is also a product that can be collected in a dust collector by closed circuit crushing (product C in Tables 3 and 6).
Contains graphite in concentrated form and serves as a raw material for graphite recovery.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明方法を説明するフローシート。 第2図は、本発明方法における微粉砕方式の概要図であ
る。 図中、(1)二ボールミル (2):前捕集槽 (3):サイクロン (4):集r1機 (5):ダクト (6):ファン (Δ):前捕集槽捕集物 (B):サイクロン捕集物 IC’):!146砿捕集物 特許出願人 日本磁力選鉱株式会社 第 1 囚 第2図
FIG. 1 is a flow sheet explaining the method of the present invention. FIG. 2 is a schematic diagram of the pulverization method in the method of the present invention. In the figure, (1) two-ball mill (2): front collection tank (3): cyclone (4): collector 1 machine (5): duct (6): fan (Δ): front collection tank collected material ( B): Cyclone collected material IC'):! 146 Copper catch patent applicant: Japan Magnetic Separation Co., Ltd. No. 1 Prisoner No. 2

Claims (1)

【特許請求の範囲】[Claims] 1、含銑鉄スラグから選別回収した金属鉄分を、破砕と
磁選を所要回数繰返して全鉄分量が90%以上になるま
で精選し、該精選物に篩分けと粒度調整、又は微粉砕と
空気分級の処理を加えることを特徴とする含銑鉄スラグ
から鉄粉を製造する方法。
1. The metal iron separated and recovered from the pig iron-containing slag is carefully selected by repeating crushing and magnetic separation the required number of times until the total iron content is 90% or more, and the selected material is subjected to sieving and particle size adjustment, or pulverization and air classification. A method for producing iron powder from pig iron-containing slag, which is characterized by subjecting it to the following treatment.
JP59222448A 1984-10-22 1984-10-22 Manufacture of iron powder from pig iron-containing slag Pending JPS6199638A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59222448A JPS6199638A (en) 1984-10-22 1984-10-22 Manufacture of iron powder from pig iron-containing slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59222448A JPS6199638A (en) 1984-10-22 1984-10-22 Manufacture of iron powder from pig iron-containing slag

Publications (1)

Publication Number Publication Date
JPS6199638A true JPS6199638A (en) 1986-05-17

Family

ID=16782559

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59222448A Pending JPS6199638A (en) 1984-10-22 1984-10-22 Manufacture of iron powder from pig iron-containing slag

Country Status (1)

Country Link
JP (1) JPS6199638A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20060023100A (en) * 2004-09-08 2006-03-13 순천대학교 산학협력단 Manufacturing of heavy materials using processed ore and granite of steel slag
JP2012529003A (en) * 2009-12-30 2012-11-15 ヒュンダイ スチール カンパニー Method for recovering valuable metals from slag
JP2015517027A (en) * 2012-03-19 2015-06-18 ミッド−アメリカン・ガナイト・インク Method and system for processing slag material
JP2021053564A (en) * 2019-09-27 2021-04-08 Jfeエンジニアリング株式会社 Waste separation/treatment method and equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20060023100A (en) * 2004-09-08 2006-03-13 순천대학교 산학협력단 Manufacturing of heavy materials using processed ore and granite of steel slag
JP2012529003A (en) * 2009-12-30 2012-11-15 ヒュンダイ スチール カンパニー Method for recovering valuable metals from slag
JP2015517027A (en) * 2012-03-19 2015-06-18 ミッド−アメリカン・ガナイト・インク Method and system for processing slag material
JP2021053564A (en) * 2019-09-27 2021-04-08 Jfeエンジニアリング株式会社 Waste separation/treatment method and equipment

Similar Documents

Publication Publication Date Title
JP2008525625A5 (en)
CN101195167B (en) Method for purifying powdered iron from steel-smelting sewage sludge coarse grain
US3368890A (en) Metal powder from cast iron chips
US4119700A (en) Production of pharmaceutical barium sulphate
US4860957A (en) Treatment of middlings
JP2626820B2 (en) Manufacturing method of high fine powder blast furnace cement
Radosavljevic et al. Mineral processing of a converter slag and its use in iron ore sintering
CA1225977A (en) Asbestos process
KR20240104078A (en) Physical recovery of valuable metal from steel slag by-product
JPH0211701A (en) Production of fe-si alloy powder
JP2015189643A (en) Sorting method for steel slag, steel slag and sorting apparatus for steel slag
CN100503092C (en) A method for extracting iron powder from converter dust
KR100797255B1 (en) Processing method of concentrate for securing high quality iron source
JPS61238901A (en) Ferromagnetic powder
KR100431499B1 (en) Method for recovering and recycling ladle slag
US2765988A (en) Reduction of iron ores
US3238037A (en) Artificial magnetic oxides
JPS59154147A (en) Magnetic reseparation of magnetized steel making slag particles
RU1774962C (en) Method of processing slags manufacture of non-magnetic and low-magnetic alloys
RU2027547C1 (en) Method to produce magnetic conducting dispersed material
KR20020051631A (en) Method for separating iron powder from slag
JPH02149606A (en) Manufacture of iron powder from converter dust
JPH11503201A (en) Reuse of metal fines
JPS6274005A (en) Manufacture of iron powder from fine converter dust
JPH0794681B2 (en) Method for producing iron powder from converter dust