JP2659596B2 - Preservation method of metal-containing iron dust powder - Google Patents

Preservation method of metal-containing iron dust powder

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Publication number
JP2659596B2
JP2659596B2 JP27386489A JP27386489A JP2659596B2 JP 2659596 B2 JP2659596 B2 JP 2659596B2 JP 27386489 A JP27386489 A JP 27386489A JP 27386489 A JP27386489 A JP 27386489A JP 2659596 B2 JP2659596 B2 JP 2659596B2
Authority
JP
Japan
Prior art keywords
metal
dust
containing iron
oxidation
iron dust
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.)
Expired - Fee Related
Application number
JP27386489A
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Japanese (ja)
Other versions
JPH03138322A (en
Inventor
望 田村
純夫 山田
啓造 田岡
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP27386489A priority Critical patent/JP2659596B2/en
Publication of JPH03138322A publication Critical patent/JPH03138322A/en
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Expired - Fee Related legal-status Critical Current

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    • 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

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、未燃焼排ガス回収装置を具備する製鋼転炉
の回収ダスト粉等含金属鉄ダスト粉の酸化抑制保存方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION <Industrial application field> The present invention relates to a method for suppressing oxidation of metal-containing iron dust powder such as collected dust powder of a steelmaking converter provided with an unburned exhaust gas recovery device.

<従来の技術> 鋼の精錬工程、特に近年の転炉精錬工程における未燃
焼排ガス回収システムの導入に伴い、転炉での酸素吹錬
時に発生するダストは高温時に大気酸素に触れることな
く冷却,除塵,回収されるためダスト中に10〜40重量%
(以下%と略す)程度の金属鉄を含んでいる。本含金属
鉄ダスト(以下ダストと略す)中には、鉄を主体に被吹
錬鋼種に応じCr,Ni等の有価金属又は金属酸化物成分を
多く含み再利用する価値は高い。
<Prior art> With the introduction of an unburned exhaust gas recovery system in the steel refining process, especially in the converter refining process in recent years, dust generated during oxygen blowing in the converter is cooled without contact with atmospheric oxygen at high temperatures. 10 to 40% by weight in dust to be removed and collected
(Hereinafter abbreviated as%). This metal-containing iron dust (hereinafter abbreviated as dust) contains a large amount of valuable metals such as Cr and Ni or metal oxide components depending on the type of steel to be blown, mainly iron, and is highly valuable for reuse.

再利用形態としてはダストを脱水・乾燥し、転炉へ炉
頂より添加する方法が一般的である。その際のダストの
扱いとして特開昭49−109212号公報に開示されているよ
うに転炉のガス回収に当たり、散水により捕集された未
燃焼ダストをドライヤーにより乾燥する場合の加熱ガス
温度を900℃以下とするとともに、乾燥後のダストがド
ライヤー排出時における含水量を5〜10%に規制し、ダ
スト中Feの殆どをFe3O4に変えることを特徴とする転炉
未燃焼ダストの酸化処理方法がある。
As a reuse form, a method of dewatering and drying dust and adding it to a converter from the furnace top is common. As disclosed in Japanese Patent Application Laid-Open No. 49-109212, the heating gas temperature for drying the unburned dust collected by sprinkling with a dryer as disclosed in JP-A-49-109212 is 900. ℃ while less dust after drying to regulate the water content at the time of dryer exhaust in 5-10%, most oxidation converter unburned dust, characterized in that changing the Fe 3 O 4 of dust in Fe There is a processing method.

しかしながらこの方法では、(a)再利用工程でFe3O
4の還元に余分な熱エネルギーが必要となる。(b)酸
化処理に余分な熱エネルギーが必要となる。(c)転炉
等の鉄浴中への添加時Fe3O4の還元による局部的な吸熱
のため、スラグ中の鉄酸化物含有量を必要以上に増加せ
しめる等の欠点をまぬがれない。
However, in this method, (a) Fe 3 O
Extra heat energy is required for the reduction of 4 . (B) Extra heat energy is required for the oxidation treatment. (C) When added to an iron bath of a converter or the like, local heat absorption due to reduction of Fe 3 O 4 does not prevent defects such as unnecessarily increasing the iron oxide content in slag.

また、特開昭62−136534号公報開示の技術のように完
全乾燥させることにより、鉄歩留りを向上する手段も開
示されているが、保存を必要とする場合乾燥後の吸湿等
によって水分は2%程度まで上昇し酸化が生じる。
Further, there is disclosed a means for improving the iron yield by complete drying as in the technique disclosed in Japanese Patent Application Laid-Open No. 62-136534. However, when storage is required, moisture is reduced by moisture absorption after drying. % And oxidation occurs.

また、特開昭63−312920号公報開示の技術のようにア
ルカリ塩を添加し塊状とする技術もあるが、塊状化のコ
ストがかかり経済的でない。
In addition, there is a technique of adding an alkali salt to form a bulk as in the technique disclosed in Japanese Patent Application Laid-Open No. 63-129920.

<発明が解決しようとする課題> 本発明は、前記従来技術の問題を解決し、含金属ダス
ト粉を粉状のまま酸化させることなく保存するための技
術を提供するためになされたものである。
<Problems to be Solved by the Invention> The present invention has been made to solve the above-mentioned problems of the prior art and to provide a technique for preserving metal-containing dust powder in powder form without oxidizing it. .

<課題を解決するための手段> 本発明は、含金属鉄ダスト粉の水分を0.8重量%以
下として金属成分の酸化を抑制する含金属鉄ダストの保
存方法で、かつ含金属鉄ダスト粉の該ダスト中のアル
カリを添加し、該ダスト1gを100ccの水中に懸濁させた
時のpHを11以上として金属成分の酸化を抑制する含金属
鉄ダスト粉の保存方法で、かつ含金属鉄ダスト粉の保
存場所の雰囲気酸素濃度を8体積%以下として金属成分
の酸化を抑制する含金属鉄ダスト粉の保存方法で、かつ
含金属鉄ダスト粉中に水等の冷却媒体を該ダストに直
接接触せずに通過させる手段を設け、該手段中に冷却媒
体を流して該ダストを冷却し金属成分の酸化を抑制する
含金属鉄ダスト粉の保存方法で、かつ前項および
記載の方法とを用いて金属成分の酸化を抑制する含金属
鉄ダスト粉の保存方法で、さらに前項および記載
の方法とを用いて金属成分の酸化を抑制する含金属鉄ダ
スト粉の保存方法である。
<Means for Solving the Problems> The present invention relates to a method for preserving metal-containing iron dust by reducing the water content of the metal-containing iron dust to 0.8% by weight or less and suppressing the oxidation of metal components. A method for preserving metal-containing iron dust powder that suppresses oxidation of metal components by adding an alkali in the dust and setting the pH of the suspension of 1 g of the dust to 100 or more in 100 cc of water to suppress the oxidation of metal components. A method for storing metal-containing iron dust powder that suppresses oxidation of metal components by reducing the atmosphere oxygen concentration of the storage location to 8% by volume or less, and directly contacting the metal-containing dust dust with a cooling medium such as water. A method for storing metal-containing iron dust powder that suppresses the oxidation of metal components by cooling the dust by flowing a cooling medium through the means, and using the method described in the preceding section and the method. Metallic iron dust powder that suppresses oxidation of components In storage method, a further storage method for suppressing metallized iron dust powder oxidation of the metal components using the methods set forth in the preceding paragraph and wherein.

<発明をなすに至った経過および作用> 含金属鉄ダスト粉の酸化を抑制しつつ貯蔵するに当た
り、重要因子を研究検討した結果、本発明者らは以下の
知見を見出した。
<Procedures and Functions Leading to the Invention> The present inventors have found the following findings as a result of studying and examining important factors in storing metal-containing iron dust powder while suppressing oxidation.

すなわち、含金属鉄ダストの酸化反応は、水分
(%)、水素イオン濃度〔H+〕またはpH=log10 1/
〔H+〕、雰囲気酸素濃度(体積%)が高く、かつダ
スト層の高温化によって、急激に進行する。
That is, the oxidation reaction of the metal-containing iron dust is determined by water (%), hydrogen ion concentration [H + ], or pH = log10 1 /
[H + ], the atmospheric oxygen concentration (vol%) is high, and the temperature rapidly rises due to the high temperature of the dust layer.

そこで、さらに各々の要因に関し、酸化反応に及ぼす
影響を同一の転炉ダストを用いて定量的に調査した結
果、以下のことが判明した。
Then, regarding each factor, the influence on the oxidation reaction was quantitatively investigated using the same converter dust, and as a result, the following was found.

先ず水分の影響については、転炉ダスト1kgを周囲環
境を断熱下に置いて、水分量を変化させダスト温度の24
時間中の経時変化を測定し、その間の飽和到達温度を調
査した結果を第1図に示す。第1図から水分が0.8%を
超えると急激に酸化進行し、酸化発熱により200℃程度
まで温度は上昇することが判明した。
First, regarding the effect of moisture, 1 kg of converter dust was placed in an insulated environment, and the moisture content was changed to reduce the dust temperature.
FIG. 1 shows the results of measuring the change over time during the time and investigating the temperature attained during this time. From FIG. 1, it was found that when the water content exceeded 0.8%, the oxidation proceeded rapidly, and the temperature rose to about 200 ° C. due to the heat generated by the oxidation.

次に、pHの影響については、水分0.05%のダスト100g
をビーカーに入れ、pHコントロールのため0〜10gのNaO
H粉を入れ混ぜ合わせた後、水を10cc程滴下してダスト
温度変化を測定する方法によりテスト開始10分後の到達
温度を調べ、その結果を第2図に示す。第2図から明ら
かなように、pHが11より下がると酸化反応が起きてい
る。なお、酸化により発熱すれば75℃以上となる。ここ
でpHはpHコントロールしたダスト1gを100ccの水中に懸
濁させ水素イオン濃度計で測定した。
Next, regarding the effect of pH, 100 g of dust with 0.05% moisture
Into a beaker and 0-10 g of NaO for pH control.
After the H powder was mixed in, the temperature reached 10 minutes after the start of the test was examined by a method of measuring the change in dust temperature by dropping about 10 cc of water, and the results are shown in FIG. As is clear from FIG. 2, an oxidation reaction occurs when the pH falls below 11. If heat is generated by oxidation, the temperature will be 75 ° C. or higher. Here, the pH was measured with a hydrogen ion concentration meter after suspending 1 g of pH-controlled dust in 100 cc of water.

更に水分を2%としたダスト1kgを周囲環境から断
熱、かつ外気遮断状態下に置き、雰囲気供給ガスをO2
N2ガスとの混合ガスとし、ガス中のO2体積%を変化させ
て前述の場合と同様に24時間中の飽和到達温度を調べ、
その結果を第3図に示した。第3図から明らかなように
雰囲気中のO2体積%が8%を超えると急激に酸化が進
み、発熱により最高220℃まで上昇している。
Further dust 1kg was 2% moisture from the ambient environment heat insulation, and placed under the outside air cutoff state, the atmosphere feed gas and O 2
As a mixed gas with N 2 gas, the O 2 volume% in the gas was changed, and the saturation attainment temperature during 24 hours was examined in the same manner as described above.
The result is shown in FIG. As is clear from FIG. 3, when the O 2 volume% in the atmosphere exceeds 8%, the oxidation rapidly proceeds, and the temperature rises up to 220 ° C. due to heat generation.

また、上記テスト中のいずれのケースにも、水冷チュ
ーブをダスト中に挿入しチューブ内に冷却水を通過させ
ると、ダスト温度の上昇は全て抑制された。
In each case during the test, when a water-cooled tube was inserted into the dust and the cooling water was allowed to pass through the tube, all rises in the dust temperature were suppressed.

以上のことより、本発明の構成要件の作用は以下のよ
うにまとめられる。
From the above, the operation of the constituent elements of the present invention can be summarized as follows.

先ず、水分の量は0.8%以下であれば酸化反応が極め
て緩慢となり実質的に抑制される。
First, if the amount of water is 0.8% or less, the oxidation reaction becomes extremely slow and is substantially suppressed.

次に、pHのコントロールはpH11以上とすることによっ
て酸化剤であるH+イオンが減少するため酸化を抑制しう
る。
Next, the pH can be controlled by setting the pH to 11 or more, whereby H + ions as an oxidizing agent are reduced, so that oxidation can be suppressed.

更に、酸化の進行には大気中のO2が必要であるが、雰
囲気O2濃度が8体積%以下の範囲においては酸化反応が
抑制される。
Furthermore, although the progress of oxidation is required O 2 in the atmosphere, in an atmosphere O 2 concentration of 8 vol% or less oxidation reaction is suppressed.

また、いずれの場合にも酸化反応による発熱を冷却流
体により間接的に抜熱することによって反応速度を低位
に留められるため酸化が抑制される。
In any case, the heat generated by the oxidation reaction is indirectly removed by the cooling fluid, so that the reaction rate can be kept low. Therefore, the oxidation is suppressed.

ダスト中の被酸化物質は、金属分と酸化数の低い酸化
物であり、具体的にはFe,FeO,Cr,CrO等である。これら
全てをFeと考えた最も安全な場合でFeはダスト中に70%
程度存在する。これを100%Feダストとして考えれば最
も安全である。
The substance to be oxidized in the dust is an oxide having a low metal content and a low oxidation number, specifically, Fe, FeO, Cr, CrO and the like. In the safest case where all of these are considered Fe, 70% Fe in dust
Degree exists. It is safest to consider this as 100% Fe dust.

Fe+O2→Fe2O3の完全酸化を考えた場合、発熱量は175
5kcal/kg−Feである。本発熱を水冷にて抜熱する際水温
上昇を20℃と考えれば、 χkg・水/kg・Fe=1755/1000kcal/kg・℃×20℃=0.09k
g・水/kg・Fe となる。よって水冷は実質的に水が存在し流れさえすれ
ば良い。エア冷却では温度上昇を50℃とすると、100Nm3
/kg・Feとなる。反応は10hrs以上かかるので、10Nm3/hr
・kg・Fe程度必要である。冷却管の配置は密な方が抜熱
の観点から好ましいが、ダストの詰まり(棚つり)を防
止するために100mm以上のピッチが望ましい。
When considering complete oxidation of Fe + O 2 → Fe 2 O 3 , the calorific value is 175
It is 5 kcal / kg-Fe. Assuming that the water temperature rise is 20 ° C when removing the heat generated by water cooling, χkg ・ water / kg ・ Fe = 1755 / 1000kcal / kg ・ ℃ × 20 ℃ = 0.09k
g ・ water / kg ・ Fe Therefore, the water cooling only needs to substantially exist and flow. In air cooling, if the temperature rise is 50 ° C, 100Nm 3
/ kg · Fe. The reaction takes 10hrs or more, so 10Nm 3 / hr
・ Kg / Fe is required. The arrangement of the cooling pipes is preferably denser from the viewpoint of heat removal, but a pitch of 100 mm or more is desirable in order to prevent dust clogging (shelf hanging).

また、これらの方法は単独でも充分に効果があるが、
ダストを貯蔵する場所,期間により、4つの方法のいく
つかを組み合わせることにより、より一層確実な酸化反
応の抑制と効果の持続、相互の方法間のバックアップの
点より好ましいことは言うまでもないことである。
In addition, although these methods are effective alone,
Needless to say, by combining some of the four methods depending on the place and period of storing the dust, it is more preferable in terms of more reliably suppressing the oxidation reaction and maintaining the effect and backing up between the mutual methods. .

<実施例> 83TON上底吹転炉で発生するダストを、排ガス回収装
置内のベンチュリースクラバーにて水洗集塵を実施して
集塵水として回収し、シックナーにて水の一部を分離し
て高濃度スラリーとした後、フィルタープレス型の脱水
機によって水分13%のケーキ状とする。その後乾燥ドラ
イヤーによってダスト中水分を0.2〜1.5%の範囲に管理
して乾燥後、溶銑および溶鋼へのインジェクションに供
すために貯蔵ホッパーに入れ貯蔵する工程において、従
来のダスト中水分0.5〜1.5%で大気封入する方法と本発
明方法との酸化防止効果を比較した。
<Example> Dust generated in the 83TON top-bottom blower is washed and collected by a venturi scrubber in an exhaust gas collection device, collected as dust collection water, and part of the water is separated by a thickener. After making the slurry into a high-concentration slurry, the slurry is made into a cake having a water content of 13% by a filter press type dehydrator. After that, the moisture content in the dust is controlled to be in the range of 0.2 to 1.5% by a drying dryer, and after drying, it is stored in a storage hopper for injection into hot metal and molten steel. The antioxidant effects of the method of sealing in air and the method of the present invention were compared.

酸化防止効果の比較のためにホッパー内ダスト温度と
切り出し量の変化とを調査した。
In order to compare the antioxidant effect, the dust temperature in the hopper and the change of the cut-out amount were investigated.

なお、貯蔵期間としては設備の定修及び休工中の最大
3日間をあてた。
The storage period was a maximum of three days during regular maintenance and suspension of work.

また、ダスト中水分量変更は、乾燥ドライヤーの操業
条件を変えてダストを数回通しコントロールした。pHコ
ントロールにはCaO粉を使用し、ダストに混練し、水分
の多いダストの場合には混入後、さらに粉砕工程を通過
させダストを粉体の状態に維持させた。貯蔵ホッパー内
の酸素濃度コントロールは、ホッパーを気密構造に改良
し、酸素濃度をコントロールできるよう配管を設け供給
O2ガス流量・N2ガス流量によってコントロールした。す
なわち酸素濃度は市販のO2連続分析計を用いて分析しつ
つ前記O2ガス流量,N2ガス流量を調節し酸素濃度をコン
トロールした。また、水冷のためホッパーには水冷管を
径方向に10本通し、冷却水を循環できるようにした。
The moisture content in the dust was controlled by passing the dust several times by changing the operating conditions of the drying dryer. CaO powder was used for pH control, kneaded with the dust, and in the case of dust having a high moisture content, after mixing, the powder was further passed through a pulverizing step to keep the dust in a powder state. The oxygen concentration in the storage hopper is controlled by improving the hopper to an airtight structure and supplying piping to control the oxygen concentration.
It was controlled by the O 2 gas flow rate and the N 2 gas flow rate. That is, the oxygen concentration was controlled by controlling the O 2 gas flow rate and the N 2 gas flow rate while analyzing using a commercially available O 2 continuous analyzer. For water cooling, 10 water cooling tubes were passed through the hopper in the radial direction so that cooling water could be circulated.

各々の水準で2回ずつテストし、その悪い方の結果を
第1表に示す。
Each level was tested twice and the worse results are shown in Table 1.

第1表から明らかなように本発明に係る含金属鉄ダス
ト粉の保存方法によると金属成分の酸化はなく、ホッパ
ー内のダスト温度は余り上昇せず、3日後のダスト切り
出しが順調にできた。
As is clear from Table 1, according to the method for preserving metal-containing iron dust powder according to the present invention, there was no oxidation of the metal component, the dust temperature in the hopper did not rise so much, and the dust cutting out after 3 days was successfully performed. .

なお、切り出し不可のダストは、ホッパーの上蓋を開
放し、人手でショベルを用いダスト抜き作業を行うこと
となり、多大なる時間(5HR)を必要とした。また、酸
化発熱のため水素が2〜10%発生し非常に危険な状態で
あった。
For dust that cannot be cut out, the upper lid of the hopper was opened and the dust was removed manually using a shovel, which required a great deal of time (5 HR). In addition, 2 to 10% of hydrogen was generated due to heat generated by oxidation, which was a very dangerous state.

<発明の効果> 本発明方法によると、含金属鉄ダスト粉中の金属鉄分
の酸化を抑制しつつ保存できる。
<Effect of the Invention> According to the method of the present invention, it is possible to store the metal-containing iron dust powder while suppressing the oxidation of the metal iron component.

従って、再使用先で還元熱が不必要であり、かつキャ
リアーガスによるインジェクションなどの流体的扱いが
できて経済的である。
Therefore, heat of reduction is unnecessary at the reuse destination, and fluid handling such as injection with a carrier gas can be performed, which is economical.

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

第1図は、ダスト中水分と到達温度との関係を示す特性
図、第2図は、ダストのpHとテスト開始10分後の到達温
度との関係を示す特性図、第3図は、雰囲気中酸素濃度
と飽和到達濃度との関係を示す特性図である。
FIG. 1 is a characteristic diagram showing the relationship between the moisture in the dust and the attained temperature, FIG. 2 is a characteristic diagram showing the relationship between the pH of the dust and the attained temperature 10 minutes after the start of the test, and FIG. FIG. 4 is a characteristic diagram illustrating a relationship between a middle oxygen concentration and a saturation reaching concentration.

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】含金属鉄ダスト粉の水分を0.8重量%以下
として金属成分の酸化を抑制する含金属鉄ダスト粉の保
存方法。
1. A method for preserving metal-containing iron dust powder in which the moisture content of the metal-containing iron dust powder is reduced to 0.8% by weight or less to suppress oxidation of metal components.
【請求項2】含金属鉄ダスト粉の該ダスト中にアルカリ
を添加し、該ダスト1gを100ccの水中に懸濁させた時のp
Hを11以上として金属成分の酸化を抑制する含金属鉄ダ
スト粉の保存方法。
2. An alkali added to said metal-containing iron dust powder, and 1 g of said dust is suspended in 100 cc of water.
A method for storing metal-containing iron dust powder in which H is set to 11 or more to suppress oxidation of metal components.
【請求項3】含金属鉄ダスト粉の保存場所の雰囲気酸素
濃度を8体積%以下として金属成分の酸化を抑制する含
金属鉄ダスト粉の保存方法。
3. A method for storing metal-containing iron dust powder, wherein the oxygen concentration in the atmosphere at the storage location of the metal-containing iron dust powder is 8% by volume or less to suppress oxidation of metal components.
【請求項4】含金属鉄ダスト粉中に水等の冷却媒体を該
ダストに直接接触させずに通過させる手段を設け、該手
段中に冷却媒体を流して該ダストを冷却し金属成分の酸
化を抑制する含金属鉄ダスト粉の保存方法。
4. Means are provided for passing a cooling medium such as water through the metal-containing iron dust powder without directly contacting the dust, and flowing the cooling medium through the means to cool the dust and oxidize metal components. Method of preserving metal-containing dust dust.
【請求項5】請求項1および2記載の方法とを用いて金
属成分の酸化を抑制する含金属鉄ダスト粉の保存方法。
5. A method for preserving metal-containing iron dust powder using the method according to claim 1 and 2, wherein the oxidation of metal components is suppressed.
【請求項6】請求項1および3記載の方法とを用いて金
属成分の酸化を抑制する含金属鉄ダスト粉の保存方法。
6. A method for preserving metal-containing iron dust powder using the method according to claim 1 and 3, wherein the oxidation of metal components is suppressed.
【請求項7】請求項4記載の方法および請求項1,2,3,5
または6記載の方法とを用いて金属成分の酸化を抑制す
る含金属鉄ダスト粉の保存方法。
7. The method according to claim 4 and claims 1, 2, 3, 5
Or a method for preserving a metal-containing iron dust powder which suppresses oxidation of a metal component using the method according to 6.
JP27386489A 1989-10-23 1989-10-23 Preservation method of metal-containing iron dust powder Expired - Fee Related JP2659596B2 (en)

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Application Number Priority Date Filing Date Title
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JPH03138322A JPH03138322A (en) 1991-06-12
JP2659596B2 true JP2659596B2 (en) 1997-09-30

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JP2003089823A (en) * 2001-09-14 2003-03-28 Nippon Steel Corp Converter dust recycling method to rotary hearth type reducing furnace
JP2006116430A (en) * 2004-10-21 2006-05-11 Actree Corp Method for recovering dehydrated cake

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* Cited by examiner, † Cited by third party
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