JPS58185733A - Treatment of steel dust containing zinc produced in steel making for reutilizing as resources - Google Patents

Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Info

Publication number
JPS58185733A
JPS58185733A JP57069411A JP6941182A JPS58185733A JP S58185733 A JPS58185733 A JP S58185733A JP 57069411 A JP57069411 A JP 57069411A JP 6941182 A JP6941182 A JP 6941182A JP S58185733 A JPS58185733 A JP S58185733A
Authority
JP
Japan
Prior art keywords
zinc
dust
recovered
heat medium
condenser
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
JP57069411A
Other languages
Japanese (ja)
Inventor
Takashi Takeda
隆 武田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57069411A priority Critical patent/JPS58185733A/en
Publication of JPS58185733A publication Critical patent/JPS58185733A/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

  • Manufacture Of Iron (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To recover Zn from steel making dust contg. zinc by separating Zn as vapor and condensing to liq. state by heating the dust with a heat medium to allow the zinc to react with a reducing material in an induction type electric furnace provided with a condenser in a cover part. CONSTITUTION:The pellets of steel making dust contg. Zn and a reducing agent such as powder coke are charged into a reaction retort 1 consisting of a low frequency induction furnace. A heat medium 6 such as iron scrap or the like in the retort is heated inductively by low-frequency induced electric powder, and the pellets of the steel making dust and the coke are allowed to react by the heat generated by heating so that ZnO in the pellets is reduced to Zn and is evaporated as the vapor of Zn. The vapor is condensed as liquid Zn 8 in a condenser 3 provided in a cover body 2 and zinc is thus recovered. The Fe component in the dust absorbs the C in the reducting agent and adds the same as molten cast iron in a heat medium 6, thereby increasing the heat capacity of the heat medium. The formed molten slag and a part of the increasing heat medium are removed by tilting the retort 1 and again the pellets and the reducing agent are added thereto so that the Zn is reduced and recovered.

Description

【発明の詳細な説明】 この発明は酸化亜鉛および酸化鉄を主成分とする含亜鉛
製鋼ダストの再資源処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recycling zinc-containing steel dust containing zinc oxide and iron oxide as main components.

含亜鉛製鋼ダスト(以下ダストという)は鉄屑を主原料
とする電気製鋼炉の酸化精錬期に発生する一部の産業廃
棄物であるが、亜鉛や鉄と共に微量のカドミニウムを含
有しているので、未処理の状頗で投棄することは環境汚
染の点で禁止されている。このためダストは、カドミニ
ウムを除去するための処理が必要であるが、カドミニウ
ムは亜鉛と一緒に回収することかできるので、亜鉛の回
収を目的とした再資源化処理がなされている。
Zinc-containing steelmaking dust (hereinafter referred to as dust) is a part of industrial waste generated during the oxidation refining stage of electric steelmaking furnaces that use iron scrap as the main raw material, but it contains trace amounts of cadmium along with zinc and iron. Dumping untreated wood is prohibited due to environmental pollution. For this reason, the dust needs to be treated to remove cadmium, but since cadmium can be recovered together with zinc, a recycling process is performed for the purpose of recovering zinc.

例えば、ダストと還元用炭とを一緒に火炎中で加熱する
ロータリーキルン法においては亜鉛が粗酸化亜鉛として
回収される。ところが、この粗酸化亜鉛は商品価値が低
いため、再資源処理のコストが高いという欠点があった
。また同時に得られる還元鉄についても経済品位以下で
あり、鉄源として利用困雌であるため、処理コストを一
層高める結果となっていた。このため、ダスト中の亜鉛
や鉄を商品価値の高い蒸留亜鉛や溶融鋳鉄として回収す
ることのできるコストの安い処理方法の開発が望まれて
いた。
For example, in a rotary kiln method in which dust and reducing charcoal are heated together in a flame, zinc is recovered as crude zinc oxide. However, since this crude zinc oxide has a low commercial value, it has the disadvantage that the cost of recycling is high. Moreover, the reduced iron obtained at the same time is of below economic grade and cannot be used as an iron source, resulting in further increase in processing costs. Therefore, it has been desired to develop a low-cost processing method that can recover zinc and iron in dust as distilled zinc and molten cast iron, which have high commercial value.

この発明の出願人は、上記の要望を満たすことのできる
装置として、先に、誘導式電気炉と、該誘導式電気炉に
装入さiL−に誘導加熱が可能な金4からなる熱線と、
誘導加熱により赤熱または溶融された熱線に被処理物を
連続的に接触させる接触促進装置とからなる鉱物、廃棄
物等の熱間処理装置(特開FM156−40070号公
報第11!iI!施例31照)を提案した。この先願は
、都市ゴミのような雑多物からダストのような産業廃棄
物まであらゆる種類の混合物を分別することなく一緒に
処理でものを拳独に処理しようとする場合には装置が複
雑すぎるという欠点があった。このためダストのみの拳
独処B11#こおいては、汎用!4!置を利用[7ての
操業の簡易化と一層の:Iストダウンが強く望まれCい
た。
The applicant of the present invention first developed an induction electric furnace and a hot wire made of gold 4, which can be charged into the induction electric furnace and capable of induction heating, as a device that can meet the above requirements. ,
An apparatus for hot treatment of minerals, waste, etc., comprising a contact promotion device that continuously brings the object to be treated into contact with a hot wire that is red-hot or melted by induction heating (Unexamined Japanese Patent Publication No. FM156-40070 No. 11!iI!Example) 31) was proposed. The previous application argued that the device was too complex to handle all kinds of mixtures, from miscellaneous materials like municipal waste to industrial waste like dust, all at once without separating them. There were drawbacks. For this reason, Dust Only Fist Dokkoko B11# is a general purpose! 4! There was a strong desire for simplification of operations and further reduction of I/O operations using the plant.

この発明は、上記の要望をここたえるため、反応レトル
トとして汎用のるつぼ形誘導炉を利用し、先1IIIV
−おける装置の簡略化による極めて操業の簡易なしかも
コストの安い処理方法を提供するものである。
In order to meet the above demands, this invention utilizes a general-purpose crucible-shaped induction furnace as a reaction retort, and
The present invention provides a processing method that is extremely simple to operate and is low in cost due to the simplification of the equipment in the process.

すなわちこの発明は、含亜鉛製鋼ダストと還元用度とか
らなる被処理物を、I[部に凝縮器を設けた誘導式電気
炉内で金嘱からなる誘導加熱の可能な熱線によって加熱
し、含頓鉛製鋼ダストの還元されて揮発する金属類を該
凝縮器に回収すると共に他の揮発することのない金属類
を炉内に回収するようにしたことを特徴とする含亜鉛製
鋼ダストの再am化処理方法である。
That is, the present invention heats a material to be treated consisting of zinc-containing steel dust and reduction grade in an induction electric furnace equipped with a condenser in part I using a hot wire made of metal and capable of induction heating, Recycling of zinc-containing steel dust, characterized in that metals that are reduced and volatilized from lead-containing steel dust are collected in the condenser, and other metals that do not volatilize are collected in the furnace. This is an am processing method.

この発明において、11導炉は高周波または低周波のい
ずれのものも用いることかできるが、操業開始用熱線が
残湯がある半連続処理の場合には鋳鉄溶解用の容量1〜
10トン程度の低周波誘導炉が有利であり、また操業開
始用熱線が鉄屑であるパッチ処理の場合には高周波誘導
炉が望ましいものである。一方ダストは、ロータリーキ
ルン法におけると同様に反応性および取扱性において、
5〜20閤程度に−・レタイジングされているものが好
ましい。また還元用度は、その径が2〜2o劇)いい、
)、やウォ□よ3,7ア、−8゜いオ。。
In this invention, the induction furnace No. 11 can be either high frequency or low frequency, but in the case of semi-continuous processing where there is residual metal, the hot wire for starting operation has a capacity of 1 to 1 for melting cast iron.
A low frequency induction furnace of about 10 tons is advantageous, and a high frequency induction furnace is preferred in the case of patch processing where the starting hot wire is scrap iron. On the other hand, dust has the same reactivity and ease of handling as in the rotary kiln method.
Preferably, it is resized to about 5 to 20 pieces. In addition, the degree of reduction is good (diameter is 2 to 2 degrees),
), Yawo □yo 3,7a, -8゜o. .

使用することかでざる。更にまた凝縮器は、公知の水平
レトルト法におけると同様に、単なる耐火物の箱状容器
で充分であるが、黒鉛からなる公知スプフッVユコンデ
ンサーを用いることもできる以下にこの発明の突施例を
図面によって説明する。第1実施例は低周波誘導炉によ
る半連続処理の例であり、第1図にこの発明に使用する
反応レトルトを示す。レトルトの本体部1は鋳鉄溶解用
として公知のるつぼ形紙周波誘導炉であり、その上端に
は密封用モルタルを介して蓋部2が載設されており、ま
た出湯fl l mには着脱自在ケこ蓋栓1bが設けら
れている9上記の8部2には被処理物の供給1] 2 
aとガス排出1】2bとが設けられており、そのト面に
は供給]]2aに連通して被処理物供給ホッパ5が設け
られており、またガス排出口2bに1!!通1.て1耐
火物製箱伏σdiからなる凝縮器311尚状1トからな
る7°IJ LJ 7グ4とが直列に設けらjしている
。fニジて供給ホッパ5へは2本のスプリノク゛フィー
ダ< tW示されていない)によりダストとコークスゲ
リーズとを各4所定の比率で供゛給Cることができる。
There is no need to use it. Furthermore, as in the known horizontal retort method, a simple refractory box-like container is sufficient as the condenser, but a known spruce-up condenser made of graphite may also be used. will be explained using drawings. The first embodiment is an example of semi-continuous treatment using a low frequency induction furnace, and FIG. 1 shows a reaction retort used in the present invention. The main body part 1 of the retort is a crucible-shaped paper frequency induction furnace known for melting cast iron, and a lid part 2 is mounted on the upper end of the retort through a sealing mortar, and the tap water fl m is detachable. The above-mentioned 8 part 2 is provided with a lid plug 1b.
A and a gas discharge port 1]]2b are provided, and a workpiece supply hopper 5 is provided on the top surface thereof in communication with the supply]]2a, and a gas discharge port 1! ! 1. A condenser 311 made of a refractory box and a 7° IJ LJ 7 made of a refractory box σdi are provided in series. Then, dust and coke gel can be supplied to the supply hopper 5 at a predetermined ratio by two splinter feeders (not shown).

上記の反しレトルiにおい“C1績業の開始の際tこは
スターrイノググロ7りの溶解にょる溶湯をPvIkと
し、次回以降には残湯を熱線とするものであり、炉谷の
20〜30%程度の熱線層6を形成する。次に熱線層6
の上に、ダストとコークスプリ ズとを7対3の比率で
混合した被処理物7を供給ホッパ5から供給する。その
結果ダスト中の酸化亜鉛は還元され揮発12て曲鉛魚気
となり、この亜鉛蒸気は一酸化伏素ガ7および二酸化#
′索ガスと共にガス排出口2bから凝縮器3に送られ、
冷却されて液化し、液状亜鉛8として回収される。
On the other hand, when starting the "C1 performance," the molten metal from Star R Inogugro 7 is used as PvIk, and from the next time onwards, the remaining melt is used as hot wire. A heat ray layer 6 of about 30% is formed.Next, a heat ray layer 6 is formed.
A material to be treated 7 containing a mixture of dust and coke spritz at a ratio of 7:3 is supplied from the supply hopper 5 onto the surface of the hopper. As a result, the zinc oxide in the dust is reduced and volatilized to turn into benthic acid.
It is sent to the condenser 3 from the gas outlet 2b together with the search gas,
It is cooled, liquefied, and recovered as liquid zinc 8.

また凝縮器3で液化できなかった一部の亜鉛はプロロン
グ4に亜鉛末として回収され、排ガスはプロロング4の
ガス排出口4aから大気中に排出される。なおりドミニ
ウムはその際に亜鉛と同時tこ回収されることはもちろ
んである。
Further, part of the zinc that cannot be liquefied in the condenser 3 is recovered as zinc powder in the prolong 4, and the exhaust gas is discharged into the atmosphere from the gas outlet 4a of the prolong 4. Of course, the dominium is recovered at the same time as the zinc.

一方、ダスト中の酸化鉄は還元の際に炭素を吸収して溶
融しスラグと分離して鋳鉄となり、この鋳鉄が熱媒とし
て作用するので、熱媒が生成した状態となり、生成熱媒
を形成して熱媒の総量を増大させる。その結果、熱媒か
らの熱の供給速度が増し、ダストは高速tこ処理される
。このようにして熱媒としての溶湯とスラグとが炉容の
約80%程度に増加した時点で炉体を傾動し、次回の熱
媒を炉内に残して増量分を出湯することによりWIM鋳
鉄が回収される。
On the other hand, the iron oxide in the dust absorbs carbon during reduction, melts it, and separates from the slag to form cast iron.This cast iron acts as a heating medium, so a heating medium is generated, forming a generated heating medium. to increase the total amount of heat transfer medium. As a result, the rate of supply of heat from the heating medium increases, and the dust is processed at a high speed. In this way, when the molten metal and slag as a heating medium have increased to about 80% of the furnace volume, the furnace body is tilted, and the next heating medium is left in the furnace and the increased amount is tapped out. is collected.

次に示す第2実施例は、操業開始用無謀が被処理物と同
時に装入の鉄屑であり、高周波誘導炉によるパッチ処理
の例であるが、これを第1図によって説明する。被処理
物を炉容の約60%程度に練入したのち少量の鉄屑を装
入し、その上に再び被処理物を装入する。そして蓋部2
を閉じて通電すると鉄屑が誘導加熱され、周囲の被処理
物を加熱し還元しながら溶融する。この溶融による溶滴
が被処理物の中を降下しながら全体を溶融し、第1実施
例と同様にして亜鉛が回収され、また全量比1こより鋳
鉄が回収される。
The second embodiment shown below is an example in which iron scrap is charged at the same time as the object to be processed, and patch processing is performed using a high frequency induction furnace. This will be explained with reference to FIG. 1. After the workpiece is mixed to about 60% of the furnace volume, a small amount of iron scrap is charged, and the workpiece is again charged on top of it. and lid part 2
When closed and energized, the iron scraps are heated by induction, heating and reducing the surrounding workpiece and melting it. Droplets resulting from this melting descend into the object to be treated and melt the entire object, and zinc is recovered in the same manner as in the first embodiment, and cast iron is recovered at a total ratio of 1.

以上に説明したようにこの発明は、被処理物を蓋部にこ
IJk111器を設けた誘導炉の中で熱媒を用いて加熱
するものであるから、大気との遮断が容易であり、亜鉛
や鉄を商品価値の高い金属状順で簡単に回収することが
できるものであり、このため処理コストが極めて安くし
かも操業は簡易である。
As explained above, in this invention, the object to be treated is heated using a heating medium in an induction furnace equipped with an IJk111 vessel in the lid, so it is easy to isolate it from the atmosphere, and zinc It is possible to easily recover metals and iron with high commercial value, and therefore the processing cost is extremely low and the operation is simple.

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

第1図はこの発明の実施例の反応し?/L−トである。 1 @4式電気炉からなるレトルト本体部、la   
:出湯口、1b:g栓、2′蓋部、2a;被処理物供#
日、2b:ガス排出口、3:m縮器、4:プロロング、
4a5プロロングのガス排出口、5被処理物供給ホツパ
、6 熱媒層、7°被処理物、8:液状亜鉛 特許出願人  武  1)    −一/−季 昇 1 図
FIG. 1 shows the reaction of an embodiment of this invention? /L-to. 1 @Retort main body consisting of 4-type electric furnace, la
: Tap spout, 1b: G stopper, 2' lid, 2a; Processing material supply #
day, 2b: gas outlet, 3: m condenser, 4: prolong,
4a5 Prolong gas outlet, 5 Processing material supply hopper, 6 Heat medium layer, 7° Processing object, 8: Liquid zinc patent applicant Takeshi 1) -1/- Kisho 1 Fig.

Claims (1)

【特許請求の範囲】 〔1〕含亜鉛製鋼ダストと還元用炭とからなる被処理物
を、蓋部に凝縮器を設けた誘導式電気炉内で金属からな
る誘導加熱の可能な熱線によって加熱し、含亜鉛製鋼ダ
ストの還元されて揮発する金属類を該凝縮器に回収する
と共に他の揮発することのない金属類を炉内に回収する
ようにしたことを特徴とする含亜鉛製鋼ダストの再資源
化処理方法。 (2)炉内に回収の金属類からなる生成熱線によって熱
線の総量を増量させ、被処理物への熱供給速度を加速さ
せながら加熱する特許請求の範囲第1項に記載の含亜鉛
製鋼ダストの再資源化処理方法。 (3〕該生成熱謀によって増量の熱線を回収金属として
出湯の際にその一部を残湯し、次回の操業開始用熱線と
して残湯出湯しながら半連続的に処理する特許請求の範
囲第1項または第2項に記載の含血鉛製鋼ダストの再資
源化処理方法。 (4〕被処理物と同時−こ装入の鉄屑からなる操業開始
用熱線と、回収金属からなる該生成熱線とを共に全量出
湯してパッチ処理する特許請求の範囲第1項または第2
項に記載の含亜鉛製鋼ダストの内置1ヒ処増方法。
[Scope of Claims] [1] A workpiece consisting of zinc-containing steel dust and reducing carbon is heated in an induction electric furnace equipped with a condenser in the lid using a hot wire made of metal capable of induction heating. The zinc-containing steel dust is characterized in that metals that are reduced and volatilized from the zinc-containing steel dust are collected in the condenser, and other metals that do not volatilize are collected in the furnace. Recycling processing method. (2) The zinc-containing steel dust according to claim 1, which is heated by increasing the total amount of heat rays generated from recovered metals in the furnace and accelerating the rate of heat supply to the object to be treated. recycling method. (3) The increased amount of hot wire generated by the heat generation strategy is used as recovered metal, a part of which is left as a residual metal when tapping the hot water, and is processed semi-continuously while tapping the remaining hot water as the hot wire for starting the next operation. The method for recycling blood-containing lead steelmaking dust according to item 1 or 2. (4) A hot wire for starting operation consisting of iron scrap charged simultaneously with the material to be treated, and the generation consisting of recovered metal. Claim 1 or 2, in which patch treatment is performed by discharging the entire amount of hot water together with the hot wire.
1. A method for internal treatment of zinc-containing steel dust as described in Section 1.
JP57069411A 1982-04-23 1982-04-23 Treatment of steel dust containing zinc produced in steel making for reutilizing as resources Pending JPS58185733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57069411A JPS58185733A (en) 1982-04-23 1982-04-23 Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57069411A JPS58185733A (en) 1982-04-23 1982-04-23 Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Publications (1)

Publication Number Publication Date
JPS58185733A true JPS58185733A (en) 1983-10-29

Family

ID=13401832

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57069411A Pending JPS58185733A (en) 1982-04-23 1982-04-23 Treatment of steel dust containing zinc produced in steel making for reutilizing as resources

Country Status (1)

Country Link
JP (1) JPS58185733A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60251234A (en) * 1984-05-25 1985-12-11 Sumitomo Heavy Ind Ltd Method for recovering valuable metal from iron dust containing high zinc
JPS6167726A (en) * 1984-09-11 1986-04-07 Sumitomo Heavy Ind Ltd Method for collecting valued metals from iron dust including highly zinc
JP2008291292A (en) * 2007-05-23 2008-12-04 Takeshi Azagami Method for manufacturing molten zinc

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60251234A (en) * 1984-05-25 1985-12-11 Sumitomo Heavy Ind Ltd Method for recovering valuable metal from iron dust containing high zinc
JPS6167726A (en) * 1984-09-11 1986-04-07 Sumitomo Heavy Ind Ltd Method for collecting valued metals from iron dust including highly zinc
JPS6348934B2 (en) * 1984-09-11 1988-10-03 Sumitomo Heavy Industries
JP2008291292A (en) * 2007-05-23 2008-12-04 Takeshi Azagami Method for manufacturing molten zinc

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