JPS60251234A - Method for recovering valuable metal from iron dust containing high zinc - Google Patents

Method for recovering valuable metal from iron dust containing high zinc

Info

Publication number
JPS60251234A
JPS60251234A JP59106188A JP10618884A JPS60251234A JP S60251234 A JPS60251234 A JP S60251234A JP 59106188 A JP59106188 A JP 59106188A JP 10618884 A JP10618884 A JP 10618884A JP S60251234 A JPS60251234 A JP S60251234A
Authority
JP
Japan
Prior art keywords
zinc
iron
pellets
lead
reduced
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
JP59106188A
Other languages
Japanese (ja)
Inventor
Toshio Matsuoka
松岡 俊雄
Shinichi Kurozu
黒豆 伸一
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP59106188A priority Critical patent/JPS60251234A/en
Publication of JPS60251234A publication Critical patent/JPS60251234A/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

Abstract

PURPOSE:To obtain crude zinc by means of distillation and separation of zinc and to recover iron and lead by means of specific gravity separation by pelletizing iron dust contg. high lead which is produced in an electric steel making process together with a carbonaceous reducing agent, melting and reducing the pellets. CONSTITUTION:The dust D contg. 25-30% Fe, 20-25% Zn and 3-4% Pb which is produced from an electric steel making factory is mixed with a carbonaceous reducing agent C such as coke and granulated to pellets Pe with a granulator 1. After removing the water from the pellets with a drier 2, these are stored and fed to a preheater 3 to be preheated and fed to a low frequency induction furnace 4 to reduce the oxides of Fe, Zn and Pb respectively. The reduced Fe is taken out as molten iron and desulfurized together with flux Fl in a desulfurizing furnace 5. The reduced Pb is separated from the molten iron by means of specific gravity difference and fed to a forging machine 7 as crude lead. The reduced Zn is evaporated and entered into a zinc condenser 8 together with gaseous CO and intermediately cooled with air A to be condensed as crude zinc for recovery.

Description

【発明の詳細な説明】 く産業上の利用分野〉 この発明は、電気炉製鋼で発生する高亜鉛含鉄ダストか
ら亜鉛、鉄などの有価金属を回収する方法化間するもの
である。
[Detailed Description of the Invention] Industrial Application Fields The present invention provides a method for recovering valuable metals such as zinc and iron from high-zinc iron-containing dust generated in electric furnace steelmaking.

〈従来技術〉 電気炉においては発生するダストを集塵機により捕集し
ているが、そのダスト量は通常粗鋼(1) 18り の3〜5%に当り、さらに、その成分は鉄25〜30%
、亜鉛20〜25チ、鉛5〜4チと多量の有価金属を含
有しているにもかかわらず、小規模でかつ簡易な回収方
法がないため、特定の精錬メーカーξこ無償で引き渡し
ているのが現状である。
<Prior art> The dust generated in an electric furnace is collected by a dust collector, but the amount of dust is usually 3 to 5% of crude steel (1) 18, and its composition is 25 to 30% of iron.
Although it contains a large amount of valuable metals, such as 20 to 25 tres of zinc and 5 to 4 tres of lead, it is handed over to a specific smelting manufacturer free of charge because it is small-scale and there is no easy recovery method. is the current situation.

このような回収方法としては、ロータリキルン−溶鉱炉
法、あるいは、最近プラズマ熱を利用した処理法が提案
されているが、いずれも処理プロセスの複雑性力よび処
理コストが高い等多くの問題を有している。
As such recovery methods, the rotary kiln-blast furnace method and the recent treatment method using plasma heat have been proposed, but both have many problems such as the complexity of the treatment process and the high treatment cost. are doing.

〈発明の目的〉 この発明は、前述のような現状に艦みて提案されたもの
で、その目的は、高亜鉛含鉄ダストから有価金属を容易
にかつ低い処理エネルギーで回収し得る有価金属回収方
法を提供することにある。
<Purpose of the Invention> This invention was proposed in view of the current situation as described above, and its purpose is to provide a method for recovering valuable metals that can easily recover valuable metals from high-zinc iron-containing dust with low processing energy. It is about providing.

〈発明の構成〉 この発明に係る有価金属回収方法は、高亜鉛含鉄ダスト
にコークスなどの炭素質固体還元剤(2) を添加した後゛、造粒してペレットにし、このペレット
を乾燥・予熱した後、誘導炉で溶融・還元させ、亜鉛は
蒸留により分離して粗亜鉛として回収し、鉄と鉛は比重
分離して鉄は溶融銑鉄として、鉛は粗鉛として回収し、
高亜鉛含鉄ダストから亜鉛、鉄などの有価金属を賽易に
かつ低い処理エネルギで回収できるようにしたものであ
る。
<Structure of the Invention> The method for recovering valuable metals according to the present invention involves adding a carbonaceous solid reducing agent (2) such as coke to high-zinc iron-containing dust, granulating it into pellets, and drying and preheating the pellets. After that, it is melted and reduced in an induction furnace, the zinc is separated by distillation and recovered as crude zinc, the iron and lead are separated by specific gravity, and the iron is recovered as molten pig iron and the lead is recovered as crude lead.
This makes it possible to easily recover valuable metals such as zinc and iron from high-zinc iron-containing dust with low processing energy.

〈実施例〉 以下、この発明を図示する一実施例に基づいて説明する
<Example> The present invention will be described below based on an illustrative example.

電気炉から回収した高亜鉛含鉄ダストDは、還元および
銑鉄に必要な炭素量を付加すべくコークス0等の炭素質
固体還元剤が添加された後、造粒機1で6〜15sus
のペレットPeζζ造粒される。
The high-zinc iron-containing dust D recovered from the electric furnace is reduced to 6 to 15 sus in a granulator 1 after a carbonaceous solid reducing agent such as coke 0 is added to reduce it and add the necessary amount of carbon to the pig iron.
The pellets Peζζ are granulated.

造粒されたペレットPaは、シャフトタイプの乾燥@2
に送られ、水分が除去された後、貯蔵・予熱器3に送ら
れる。
Granulated pellets Pa are dried in shaft type @2
After moisture is removed, the water is sent to the storage/preheater 3.

予熱されたペレツ)Paは、低周波誘導炉4に投入され
、銑酸化物、亜鉛酸化物、鉛酸化物は還元・溶融され、
残りの金属酸化物は大部分スラグs1を形成する。
The preheated pellets) Pa are put into a low frequency induction furnace 4, where pig oxides, zinc oxides, and lead oxides are reduced and melted.
The remaining metal oxide mostly forms slag s1.

還元された鉄Fθは、溶銑(約4%O)として誘導炉4
から排出され、必要に応じて脱硫装置5を通してフラッ
クスF1により脱硫させた後、電気炉6ヘホツトチヤー
ジされる。
The reduced iron Fθ is transferred to induction furnace 4 as hot metal (approximately 4% O).
After being desulfurized by flux F1 through a desulfurization device 5 if necessary, it is hot-charged into an electric furnace 6.

生成したスラグは誘導炉iこ通電したま才攪拌状態で溶
銑とともに抜き出すか、通電を止めて一時的こと静置し
、高炉で通常行なわれているごとく炉側の別々の排出口
より排出される。
The generated slag is extracted from the induction furnace together with the hot metal while it is being energized and stirred, or it is left to stand still temporarily with the energization turned off, and then discharged from separate discharge ports on the furnace side, as is normally done in blast furnaces. .

還元された鉛pbは、比重が比較的大きいため、溶銑と
比重分離し、炉下部にたまったのを定期的に抜き取り、
粗鉛として鉛鋳造機7へ送る。
Since the reduced lead PB has a relatively high specific gravity, it is separated from the hot metal by specific gravity, and the accumulated part at the bottom of the furnace is periodically extracted.
It is sent to the lead casting machine 7 as crude lead.

還元された亜鉛Znは、沸点が比較的低いため、溶融・
蒸発し、還元ガス00とともにガス状態で亜鉛凝縮器8
−こ導びかれ、空気Aによる間接冷却により液状物とし
て凝縮し、亜鉛鋳造機9に連続して送られ、粗亜鉛とし
て回収される。
Reduced zinc Zn has a relatively low boiling point, so it cannot be melted or
Zinc condenser 8 in gaseous state with evaporated and reducing gas 00
- It is guided, condensed as a liquid by indirect cooling with air A, and continuously sent to the zinc casting machine 9, where it is recovered as crude zinc.

亜鉛凝縮器8を出た還元ガス00は、さらに貯蔵・予熱
器3#こ送られ、ペレットPaの予熱器こその顕熱が利
用された後、ガスホルダー10に送られるとともにその
一部がペレット乾燥用の燃料として燃焼炉11に送られ
る。
The reducing gas 00 that has exited the zinc condenser 8 is further sent to the storage/preheater 3#, where the sensible heat of the preheater for the pellets Pa is utilized, and then sent to the gas holder 10, where part of it is converted into pellets. It is sent to the combustion furnace 11 as a drying fuel.

また、亜鉛凝縮器8で熱交換した空気も燃焼炉11に送
られ、還元ガス00の燃焼用詔よびペレット乾燥用の熱
源として利用される。
Furthermore, the air heat-exchanged in the zinc condenser 8 is also sent to the combustion furnace 11 and used as a heat source for burning the reducing gas 00 and drying the pellets.

なお、乾燥機2の排ガスGは、一部が燃焼炉11にリサ
イクルされ、脱硫装置12において脱硫され、集塵装置
15により除塵された後、外部へ排出される。
A portion of the exhaust gas G from the dryer 2 is recycled to the combustion furnace 11, desulfurized by the desulfurizer 12, removed by the dust collector 15, and then discharged to the outside.

〈発明の効果〉 前述のとおり、この発明によれば高亜鉛含鉄ダストに炭
素質固体還元剤を添加し、ペレタイジング・乾燥・予熱
した後、誘導炉で溶融−還元させ、亜鉛は蒸留により分
離して粗亜鉛として回収し、鉄と鉛は比重分離して鉄は
溶融銑鉄として、鉛は粗鉛として回収し、誘導炉の排ガ
スをペレットの乾燥予熱に利用するようにしたため、次
のような効果を奏する。
<Effects of the Invention> As described above, according to the present invention, a carbonaceous solid reducing agent is added to high zinc-containing iron dust, and after pelletizing, drying, and preheating, it is melted and reduced in an induction furnace, and zinc is separated by distillation. iron and lead are separated by specific gravity, iron is recovered as molten pig iron, and lead is recovered as crude lead.The exhaust gas from the induction furnace is used to dry and preheat the pellets, resulting in the following effects: play.

(1)誘導炉は、攪拌力が大きく、かつ炉体を気密性の
ある構造にすることが容易であるため、ペレットの溶解
、還元、亜鉛の蒸留こと適しており、有価金属を容易に
回収することができる。
(1) Induction furnaces have a large stirring power and are easy to make the furnace body have an airtight structure, so they are suitable for melting pellets, reduction, and distilling zinc, and can easily recover valuable metals. can do.

(II) 誘導炉の排ガスをペレットの乾燥・予熱に有
効ζこ利用するとともに還元生成ガス00の大部分を系
外の燃料等に利用しているので、(I)と和才って低い
処理エネルギーで有価金属の回収を行なうことができる
(II) Since the exhaust gas of the induction furnace is effectively used for drying and preheating the pellets, and most of the reduction product gas is used as fuel outside the system, the processing efficiency is lower than in (I). Valuable metals can be recovered using energy.

611)鉄分は溶銑として回収し電気炉にホットチャー
ジすれば銑鉄の顕熱を有効に利用できる。
611) If iron is recovered as hot metal and hot-charged into an electric furnace, the sensible heat of the pig iron can be effectively used.

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

図面はこの発明番と係る有価金属回収方法を実施するた
めの装置のフローチャートである。 D・・高亜鉛含鉄ダスト、0・・コークス、Pa・寺ペ
レット、 Fe・・鉄、Zrz・亜鉛、PI) 。 ・鉛、 74・・フラックス、COI・還元ガス、A・
・空気、1・・造粒機、2・・乾燥機、3・・貯蔵・予
熱器、4・・誘導炉、5・・脱硫装置、6・・電気炉、
7・・鉛鋳造機、8・拳亜鉛凝縮器、9・・亜鉛鋳造機
、10・壷ガスホルダー、11−・燃焼炉、12−・脱
硫装置、13拳・集塵装置。 (7)
The drawing is a flowchart of an apparatus for carrying out the valuable metal recovery method according to this invention number. D...high zinc iron-containing dust, 0...coke, Pa/temperature pellets, Fe...iron, Zrz/zinc, PI).・Lead, 74...Flux, COI/Reducing gas, A.
・Air, 1.. Granulator, 2.. Dryer, 3.. Storage/preheater, 4.. Induction furnace, 5.. Desulfurization equipment, 6.. Electric furnace.
7. Lead casting machine, 8. Zinc condenser, 9. Zinc casting machine, 10. Gas holder, 11. Combustion furnace, 12. Desulfurization equipment, 13. Dust collector. (7)

Claims (1)

【特許請求の範囲】[Claims] (1) 高亜鉛含鉄ダストに炭素質固体還元剤を添加し
た後、造粒してペレットにし、このペレットを乾燥・予
熱した後、誘導炉で溶融・還元させ、亜鉛は蒸留により
分離して粗亜鉛として回収し、鉄と鉛は比重分離して鉄
は溶融銑鉄として、鉛は粗鉛として回収することを特徴
とする高亜鉛含鉄ダストからの有価金属回収方法。
(1) After adding a carbonaceous solid reducing agent to high-zinc iron-containing dust, it is granulated into pellets. After drying and preheating the pellets, they are melted and reduced in an induction furnace, and the zinc is separated by distillation to form a crude product. A method for recovering valuable metals from high zinc-containing iron dust, which is characterized in that zinc is recovered, iron and lead are separated by specific gravity, iron is recovered as molten pig iron, and lead is recovered as crude lead.
JP59106188A 1984-05-25 1984-05-25 Method for recovering valuable metal from iron dust containing high zinc Pending JPS60251234A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59106188A JPS60251234A (en) 1984-05-25 1984-05-25 Method for recovering valuable metal from iron dust containing high zinc

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59106188A JPS60251234A (en) 1984-05-25 1984-05-25 Method for recovering valuable metal from iron dust containing high zinc

Publications (1)

Publication Number Publication Date
JPS60251234A true JPS60251234A (en) 1985-12-11

Family

ID=14427220

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59106188A Pending JPS60251234A (en) 1984-05-25 1984-05-25 Method for recovering valuable metal from iron dust containing high zinc

Country Status (1)

Country Link
JP (1) JPS60251234A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5279643A (en) * 1992-01-17 1994-01-18 Yasuo Kaneko Process for recovering valuable metals from an iron dust
KR100400416B1 (en) * 1999-06-11 2003-10-04 주식회사 포스코 LAW Zn SLUGE SEPARATING APPARATUS OF FURNACE THICKER
DE10240224A1 (en) * 2002-07-29 2004-02-26 M.I.M. Hüttenwerke Duisburg Gmbh Process for the thermal recovery of zinc comprises adding a zinc-containing secondary raw material as feed material in the form of molded bricks to a shaft kiln
CN109457123A (en) * 2018-11-09 2019-03-12 中冶南方工程技术有限公司 The treatment process of iron content zinc powder dirt
PL424985A1 (en) * 2018-03-21 2019-09-23 Dobrzyński Michał P.P.H.U Stilmar Method for recovery of zinc and iron alloy from suspended metallurgical particulate matter

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58185733A (en) * 1982-04-23 1983-10-29 Takashi Takeda Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58185733A (en) * 1982-04-23 1983-10-29 Takashi Takeda Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5279643A (en) * 1992-01-17 1994-01-18 Yasuo Kaneko Process for recovering valuable metals from an iron dust
KR100400416B1 (en) * 1999-06-11 2003-10-04 주식회사 포스코 LAW Zn SLUGE SEPARATING APPARATUS OF FURNACE THICKER
DE10240224A1 (en) * 2002-07-29 2004-02-26 M.I.M. Hüttenwerke Duisburg Gmbh Process for the thermal recovery of zinc comprises adding a zinc-containing secondary raw material as feed material in the form of molded bricks to a shaft kiln
PL424985A1 (en) * 2018-03-21 2019-09-23 Dobrzyński Michał P.P.H.U Stilmar Method for recovery of zinc and iron alloy from suspended metallurgical particulate matter
CN109457123A (en) * 2018-11-09 2019-03-12 中冶南方工程技术有限公司 The treatment process of iron content zinc powder dirt

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