JPS6167726A - Method for collecting valued metals from iron dust including highly zinc - Google Patents

Method for collecting valued metals from iron dust including highly zinc

Info

Publication number
JPS6167726A
JPS6167726A JP59190185A JP19018584A JPS6167726A JP S6167726 A JPS6167726 A JP S6167726A JP 59190185 A JP59190185 A JP 59190185A JP 19018584 A JP19018584 A JP 19018584A JP S6167726 A JPS6167726 A JP S6167726A
Authority
JP
Japan
Prior art keywords
zinc
iron
lead
including highly
molten
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
JP59190185A
Other languages
Japanese (ja)
Other versions
JPS6348934B2 (en
Inventor
Toshio Matsuoka
松岡 俊雄
Shinichi Kuromame
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 JP59190185A priority Critical patent/JPS6167726A/en
Priority to KR1019850006297A priority patent/KR910000013B1/en
Priority to US06/774,503 priority patent/US4612041A/en
Priority to DE8585111448T priority patent/DE3584865D1/en
Priority to EP19850111448 priority patent/EP0174641B1/en
Priority to CA000490303A priority patent/CA1239798A/en
Publication of JPS6167726A publication Critical patent/JPS6167726A/en
Publication of JPS6348934B2 publication Critical patent/JPS6348934B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B19/00Obtaining zinc or zinc oxide
    • C22B19/30Obtaining zinc or zinc oxide from metallic residues or scraps
    • 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 collect easily a valued metal by low energy by dissolving and deoxidizing a molten iron dust including highly zinc with a carbonaceous solid reducing agent, and separating zinc, iron and lead respectively after the iron dust including highly zinc is granulated and dried. CONSTITUTION:An iron dust including highly zinc D recollected from an electric oven is granulated by a granulating machine 1 in pellet, sent to a drying preheater 2 to remove water content and the reduced quantity due to strong heating and an amount of solid carbon in the pellet is removed by burning. This pellet is sent to a low frequency induction furnace 3 with a coke C dried by a dryer 14, each oxide of iron, zinc and lead is deoxidated and molted, and the residual metallic oxide is mostly slag Sl. The deoxidized iron is discharged as a molten iron Fe from a induction furnace 3 to take out a slag Sl from an exhaust port. The deoxidized lead Pb is gravity-separated from a molten iron and pulled out as a pig lead through a lead bank 4. The deoxidized zinc Zn is molten, evaporated and led to a zinc condensor 5 together with the deoxidated gas CO and cooled to remove impurity and collected through a cooling tub as a pig zinc.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 この発明は、例えは電気炉製鋼で発生ずる高亜鉛含鉄ダ
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 recovering valuable metals such as zinc and iron from high-zinc iron-containing dust generated, for example, in electric furnace steelmaking.

〈従来技術とその問題点〉 例えば電気炉において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の6〜5%に当
り、さらに、その成分は鉄25〜30%、亜鉛20〜2
5チ、鉛3〜4係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に引き渡して集中処理しているのが
現状である。
<Prior art and its problems> For example, dust generated in an electric furnace is collected by a dust collector, but the amount of dust is usually 6 to 5% of crude steel, and its composition is 25 to 30% iron, Zinc 20-2
Although it contains a large amount of valuable metals, such as lead 3 and 4, there is no simple recovery method on a small scale.
Currently, it is handed over to specific smelting manufacturers for centralized processing.

このような回収方法として、ロークリキルン−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および処理
コストが高い等多くの問題を有している。
As such recovery methods, the lorry kiln-blast furnace method and recently a 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. .

この発明は、前述のような現状に鑑みて提案されたもの
で、その目的は、高亜鉛含鉄コストから有価金属を容易
に且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。
This invention was proposed in view of the above-mentioned current situation, and its purpose is to provide a method for recovering valuable metals that can easily recover valuable metals from high zinc-containing iron costs with low processing energy. .

〈問題点を解決するための手段〉 この発明に係る有価金属回収方法は、高亜鉛含鉄ダスト
を造粒してペレットにし、このペレットを乾燥・予熱工
程で高温装入hスにより、ダスト中の強熱減量弁(高温
で気化する水酸化物、炭酸化物、塩化物等)を除去する
と共に、積極的にタスト中の固定炭素分を燃焼除去した
後、炭素質還元剤と共に誘導炉に投入し、誘導炉で溶融
・還元さぜ、亜鉛は蒸留により分離して粗亜鉛として、
鉄と鉛は比重分離して、鉄は溶融銑鉄として、鉛は粗鉛
として容易に且つ低い処理エネルギーで回収できるよう
にしたものである。
<Means for Solving the Problems> The method for recovering valuable metals according to the present invention is to granulate high-zinc iron-containing dust into pellets, and charge the pellets at high temperature in a drying/preheating process to remove the amount of metal in the dust. After removing the ignition loss valve (hydroxides, carbonates, chlorides, etc. that vaporize at high temperatures) and actively burning off the fixed carbon content in the tast, it is put into an induction furnace together with a carbonaceous reducing agent. The zinc is then melted and reduced in an induction furnace and separated by distillation to produce crude zinc.
Iron and lead are separated by specific gravity so that iron can be recovered as molten pig iron and lead can be recovered as crude lead easily and 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、造粒機1で
6〜15mmのペレットに造粒される。
The high-zinc iron-containing dust D recovered from the electric furnace is granulated into pellets with a size of 6 to 15 mm in a granulator 1.

造粒されたペレットは、シャフトタイプの乾燥・予熱器
2に送られ、800〜1000’Cの装入ガスにより乾
燥・予熱され、炉」二部で水分が除去された後、炉下部
の高温帯に移動しながら強熱減量弁が除去され、さらに
ペレット中の固定炭素分が燃焼除去される。ここで、固
定炭素の燃焼は、ペレットの予熱に利用されることにな
り、エネルギーの損失はない。
The granulated pellets are sent to the shaft type dryer/preheater 2, where they are dried and preheated with charging gas at 800 to 1000'C, and after removing moisture in the second part of the furnace, they are heated to a high temperature in the lower part of the furnace. While moving to the belt, the ignition loss valve is removed, and the fixed carbon content in the pellets is further burned off. Here, the combustion of fixed carbon will be used to preheat the pellets, and there is no loss of energy.

このペレットは、コークス乾燥器14により乾燥された
コークスCと共に低周波誘導炉乙に投入され、鉄酸化物
、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。
These pellets are fed into a low frequency induction furnace B along with coke C dried by the coke dryer 14, where iron oxides, zinc oxides, and lead oxides are reduced and melted, and most of the remaining metal oxides are turned into slag. Form S1.

還元された鉄は、溶融銑鉄(約4%0)Feとして誘導
炉6から排出され、後段の電気炉ヘホットチャージされ
る。
The reduced iron is discharged from the induction furnace 6 as molten pig iron (approximately 4% 0) Fe, and hot-charged to the subsequent electric furnace.

生成したスラグは、誘導炉に通電したまま撹拌状態で溶
銑と共に抜き出すか、通電を止めて一時的に静置し、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 either extracted with the hot metal while stirring while the induction furnace is energized, or the slag is left to stand temporarily with the energization turned off, and then discharged from a separate outlet 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、炉下部の鉛溜4に溜り定期的に粗鉛として
抜きとられる。
Since the reduced lead Pb has a relatively high specific gravity, it is separated from the hot metal in specific gravity, accumulates in a lead reservoir 4 in the lower part of the furnace, and is periodically extracted 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と共にガス状態で亜鉛凝縮器5に
導かれ、亜鉛循環ポンプ7により循環された溶融亜鉛に
より冷却され、液状物として凝縮し、冷却誦6で冷却、
不純物を除去された後、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
The molten zinc is evaporated and introduced into the zinc condenser 5 in a gaseous state together with the reducing gas 00, cooled by the molten zinc circulated by the zinc circulation pump 7, condensed as a liquid, and cooled in the cooling tank 6.
After removing impurities, it is recovered as crude zinc.

凝縮器5を出た還元ガスCOは、熱交換器8で燃焼用空
気と熱交換した後、集塵機9、塩素除去装置10、脱硫
装置11を経てガスホルダー12に送られ、その一部は
ペレットの乾燥・予熱の燃料として燃焼炉16に送られ
る。
The reducing gas CO exiting the condenser 5 exchanges heat with combustion air in a heat exchanger 8, and then is sent to a gas holder 12 via a dust collector 9, a chlorine removal device 10, and a desulfurization device 11, and a portion of it is converted into pellets. The fuel is sent to the combustion furnace 16 as fuel for drying and preheating.

また、熱交換器8で熱交換した空気も燃焼炉16に送ら
れ、還元ガスCOの燃焼用として利用される。
Further, the air heat exchanged with the heat exchanger 8 is also sent to the combustion furnace 16 and used for combustion of the reducing gas CO.

さらに、乾燥・予熱器2の排ガスは、コークス乾燥器1
4に導かれ、コークスの乾燥に利用された後、集塵装置
15を経て系外へ排出される。
Furthermore, the exhaust gas from the dryer/preheater 2 is transferred to the coke dryer 1.
4 and used for drying the coke, it is then discharged to the outside of the system via a dust collector 15.

〈発明の効果〉 前述のとおり、この発明によれば、高亜鉛含鉄ダストを
造粒し、乾燥・予熱工程で高温装入ガスにより、ペレッ
ト中の強熱減量弁を除去すると共に、積極的にペレット
中の固定炭素分を燃焼除去した後、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、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, high-zinc iron-containing dust is granulated, and the ignition loss valve in the pellets is removed by high-temperature charging gas in the drying/preheating process, and the ignition loss valve is actively After burning off the fixed carbon content in the pellets, they are melted and reduced in an induction furnace. Zinc is separated by distillation to produce crude zinc, iron and lead are separated by specific gravity, iron is converted to molten pig iron, and lead is converted to crude lead. This method has the following effects.

(1)誘導炉は、攪拌力が大きく、且つ炉体を気密のあ
る構造にすることが容易であるため、ペレットの溶融、
還元、亜鉛の蒸留に適しており、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 force and are easy to make the furnace body have an airtight structure.
It is suitable for reduction and distillation of zinc, and valuable metals can be easily recovered.

(li l  強熱減量弁を予め除去することにより、
ペレットを炉の溶湯中に装入した場合、バースティング
を起こすことがなく、溶湯の安定した操業が可能になり
、ダストの発生も抑制できる。
(li l By removing the ignition loss valve in advance,
When pellets are charged into molten metal in a furnace, bursting does not occur, stable operation of the molten metal is possible, and dust generation can be suppressed.

仙)ペレットの炭素分を予め燃焼することにより、ペレ
ットを予熱できる他、ペレットの還元に必要な還元剤と
しての炭素は、ペレット内に存在する炭材、所謂内炭か
ら供給されるのではなく、炉内の溶銑の炭素から供給さ
れるため、ペレット中の金属酸化物の還元は、ペレット
表面のみで起こる。そのため、内炭を有するペレツi・
が急激に高温にさらされた時に生じる急激なガス発生や
それに伴うペレットの破壊を防止することができ、溶湯
の突沸、ダストの発生を抑制できる。
By pre-combusting the carbon content of the pellets, the pellets can be preheated, and the carbon needed to reduce the pellets as a reducing agent is not supplied from the carbonaceous material present in the pellets, the so-called inner charcoal. , the reduction of metal oxides in the pellets occurs only on the pellet surface, since the carbon is supplied from the hot metal in the furnace. Therefore, Perez i.
It is possible to prevent the sudden generation of gas that occurs when the metal is suddenly exposed to high temperatures and the accompanying destruction of the pellets, and it is possible to suppress the bumping of the molten metal and the generation of dust.

(1v)鉄分は溶銑として回収し、後段の電気炉ヘホッ
トチャージすれば、溶銑の顕熱を有効に利用できる。
(1v) If the iron content is recovered as hot metal and hot-charged to the subsequent electric furnace, the sensible heat of the hot metal can be effectively used.

(■)誘導炉の排ガスをペレットの乾燥・予熱に必要な
高温ガス生成のための燃焼用空気と熱交換するとともに
、還元生成ガスの大部分を系外の燃料等に利用している
ので、(1)と相ま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。
(■) In addition to exchanging heat with the combustion air to generate the high-temperature gas necessary for drying and preheating the pellets, the exhaust gas from the induction furnace is used as fuel, etc. outside the system. Coupled with (1), valuable metals can be recovered with low processing energy.

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

図面はこの発明に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。 1・・造粒機、2・・乾燥・予熱器、ろ・・誘導炉、4
・・鉛溜、5・・亜鉛凝縮器、6・・冷却随、7・・亜
鉛循環ポンプ、8・・熱交換器、9・・集塵機、10・
・塩素除去装置、11・・脱硫装置、12・・ガスホル
ダー、13・・燃焼炉、14・・コークス乾燥機、15
・集塵装置、D・・高亜鉛言鉄タスト、C・・コークス
、S認・・スラク、Fθ・・溶融銑鉄、Zn・・溶融亜
鉛、Pl)・・溶融鉛、G・・排ガス、A・・空気。
The drawing is a flowchart of an apparatus for implementing the method for recovering valuable metals according to the present invention. 1. Granulator, 2. Drying/preheater, filter, induction furnace, 4
... Lead reservoir, 5. Zinc condenser, 6. Cooling equipment, 7. Zinc circulation pump, 8. Heat exchanger, 9. Dust collector, 10.
- Chlorine removal equipment, 11... Desulfurization equipment, 12... Gas holder, 13... Combustion furnace, 14... Coke dryer, 15
・Dust collector, D.・High zinc iron tast, C.・Coke, S-certified.・Slak, Fθ.・ Molten pig iron, Zn.・ Molten zinc, Pl)・・ Molten lead, G.・Exhaust gas, A. ··air.

Claims (1)

【特許請求の範囲】[Claims] (1)高亜鉛含鉄ダストを造粒してペレットにし、この
ペレットを乾燥・予熱してダスト中の強熱減量分を除去
するとともに、積極的にダスト中の固定炭素分を燃焼除
去した後、炭素質固体還元剤と共に誘導炉に投入し、該
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 granulating high-zinc iron-containing dust into pellets, drying and preheating the pellets to remove the ignition loss in the dust, and actively burning and removing the fixed carbon content in the dust, It is put into an induction furnace together with a carbonaceous solid reducing agent, and melted and reduced in the induction furnace. Zinc is separated by distillation and recovered as crude zinc, iron and lead are separated by specific gravity, iron is converted into molten pig iron, and lead is A method for recovering valuable metals from high zinc-containing iron dust, which is characterized by recovering crude lead.
JP59190185A 1984-09-11 1984-09-11 Method for collecting valued metals from iron dust including highly zinc Granted JPS6167726A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP59190185A JPS6167726A (en) 1984-09-11 1984-09-11 Method for collecting valued metals from iron dust including highly zinc
KR1019850006297A KR910000013B1 (en) 1984-09-11 1985-08-30 Process for recovering valuable metals from an iron dust containing a higher content of zinc
US06/774,503 US4612041A (en) 1984-09-11 1985-09-10 Process for recovering valuable metals from an iron dust containing a higher content of zinc
DE8585111448T DE3584865D1 (en) 1984-09-11 1985-09-10 METHOD FOR RECOVERING HIGH QUALITY METALS FROM IRON DUST WITH HIGH ZINC CONTENT.
EP19850111448 EP0174641B1 (en) 1984-09-11 1985-09-10 A process for recovering valuable metals from an iron dust containing a higher content of zinc
CA000490303A CA1239798A (en) 1984-09-11 1985-09-10 Process for recovering valuable metals from an iron dust containing a higher content of zinc

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59190185A JPS6167726A (en) 1984-09-11 1984-09-11 Method for collecting valued metals from iron dust including highly zinc

Publications (2)

Publication Number Publication Date
JPS6167726A true JPS6167726A (en) 1986-04-07
JPS6348934B2 JPS6348934B2 (en) 1988-10-03

Family

ID=16253863

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59190185A Granted JPS6167726A (en) 1984-09-11 1984-09-11 Method for collecting valued metals from iron dust including highly zinc

Country Status (2)

Country Link
JP (1) JPS6167726A (en)
KR (1) KR910000013B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63317618A (en) * 1987-04-21 1988-12-26 コルフ・エンジニアリング・ゲーエムベーハー Method of cooling heated material and equipment for carrying out same
JPH0754030A (en) * 1993-06-16 1995-02-28 Iscar Ltd Preparation of steel
KR100400416B1 (en) * 1999-06-11 2003-10-04 주식회사 포스코 LAW Zn SLUGE SEPARATING APPARATUS OF FURNACE THICKER

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020059012A1 (en) * 2018-09-18 2020-03-26 株式会社アプトポッド Abnormality detection device, abnormality detection system, and program

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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63317618A (en) * 1987-04-21 1988-12-26 コルフ・エンジニアリング・ゲーエムベーハー Method of cooling heated material and equipment for carrying out same
JPH0754030A (en) * 1993-06-16 1995-02-28 Iscar Ltd Preparation of steel
KR100400416B1 (en) * 1999-06-11 2003-10-04 주식회사 포스코 LAW Zn SLUGE SEPARATING APPARATUS OF FURNACE THICKER

Also Published As

Publication number Publication date
JPS6348934B2 (en) 1988-10-03
KR910000013B1 (en) 1991-01-19
KR860002584A (en) 1986-04-26

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