JPH0734149A - Evaporated zinc recovery device - Google Patents

Evaporated zinc recovery device

Info

Publication number
JPH0734149A
JPH0734149A JP19883493A JP19883493A JPH0734149A JP H0734149 A JPH0734149 A JP H0734149A JP 19883493 A JP19883493 A JP 19883493A JP 19883493 A JP19883493 A JP 19883493A JP H0734149 A JPH0734149 A JP H0734149A
Authority
JP
Japan
Prior art keywords
zinc
disk
melting furnace
vacuum
evaporated
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
JP19883493A
Other languages
Japanese (ja)
Other versions
JP3319056B2 (en
Inventor
Kenji Matsuda
謙治 松田
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries 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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP19883493A priority Critical patent/JP3319056B2/en
Publication of JPH0734149A publication Critical patent/JPH0734149A/en
Application granted granted Critical
Publication of JP3319056B2 publication Critical patent/JP3319056B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

(57)【要約】 【目的】 スクラップからの亜鉛の回収を、安価な設備
で効率よく行う。 【構成】 容器本体1と容器蓋体2からなる真空容器4
に、誘導溶解炉5を収容させて、簡易型の真空溶解装置
8を構成する。容器蓋体2内に円板12を昇降及び回転
可能に配置する。容器蓋体2の内周面部に捕集樋14を
設ける。溶解炉5内に装入したスクラップを加熱し、蒸
発した亜鉛を、最上部に位置させておいた円板12の下
面に蒸着させる。しかる後、円板12を下降させ、溶銑
の熱で蒸着亜鉛を融解し、融解亜鉛を円板12の回転で
飛ばして捕集樋14で捕集する。
(57) [Summary] [Purpose] To recover zinc from scrap efficiently with inexpensive equipment. [Structure] Vacuum container 4 including container body 1 and container lid 2
Then, the induction melting furnace 5 is housed therein, and a simple vacuum melting device 8 is configured. The disk 12 is arranged in the container lid 2 so as to be vertically movable and rotatable. A collection trough 14 is provided on the inner peripheral surface of the container lid 2. The scrap charged in the melting furnace 5 is heated, and the evaporated zinc is vapor-deposited on the lower surface of the disk 12 placed at the top. Then, the disk 12 is lowered, the vaporized zinc is melted by the heat of the hot metal, and the molten zinc is blown off by the rotation of the disk 12 and collected by the collecting trough 14.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は自動車用鋼板の打ち抜き
残材等の廃材をエンジンボディ等を鋳造するための原料
として再利用するに際して問題となっている脱亜鉛を高
い効率で実現し、且つ亜鉛を金属亜鉛として回収できる
ようにした蒸発亜鉛回収装置に関するものである。
BACKGROUND OF THE INVENTION The present invention realizes a high efficiency of dezincification, which is a problem when reusing waste materials such as punching residual materials of automobile steel sheets as raw materials for casting engine bodies and the like, and The present invention relates to an evaporated zinc recovery device capable of recovering zinc as metallic zinc.

【0002】[0002]

【従来の技術】鉱物資源に乏しい我が国では、スクラッ
プの再生は重要な課題であり、鉄鋼材料のスクラップリ
サイクルについても種々の試みがなされている。その中
で、耐食性確保のために亜鉛メッキされた亜鉛メッキ鋼
板のスクラップは、高炉、キュポラあるいは電気製鋼炉
等である程度まで用いられてきたが、ダストへの亜鉛又
は酸化亜鉛の移行、炉体耐火物の亜鉛による侵食という
問題が知られている。
2. Description of the Related Art In Japan, where mineral resources are scarce, recycling scrap is an important issue, and various attempts have been made to recycle scrap of steel materials. Among them, scraps of galvanized steel sheets galvanized to ensure corrosion resistance have been used to some extent in blast furnaces, cupolas, electric steelmaking furnaces, etc., but zinc or zinc oxide transfer to dust, furnace body fire resistance The problem of zinc erosion of materials is known.

【0003】ところで、近年の自動車生産台数の大きな
伸びは、自動車メーカー内の亜鉛メッキ鋼板の打ち抜き
残材等のスクラップ増加をもたらしているが、昨今の公
害規制やその他により、製品鋳鉄への亜鉛の混入が少な
いキュポラの廃却が進んでしまった今日では、エンジン
ボディ等の鋳鉄の原料として、インハウススクラップで
ある打ち抜き残材を利用できる割合は逆に低下してい
る。これは、キュポラに代って採用される低周波溶解炉
の場合、溶銑への亜鉛の残留がキュポラ銑に比して多
く、この亜鉛が黒鉛の球状化や安定した酸化被膜の形成
を阻害し、鋳鉄の品質を劣化させるためである。
By the way, the recent great increase in the number of automobiles produced has led to an increase in scraps such as punching residual materials of galvanized steel sheets in automobile manufacturers. However, due to recent pollution regulations and other factors, zinc in product cast iron is Nowadays, with the progress of abandonment of cupola, which contains a small amount of contaminants, the rate at which punching residual material, which is in-house scrap, can be used as a raw material for cast iron such as engine bodies is decreasing. This is because in the case of the low-frequency melting furnace used instead of cupola, the amount of zinc remaining in the hot metal is higher than that of cupola hot metal, and this zinc hinders the spheroidization of graphite and the formation of a stable oxide film. , To deteriorate the quality of cast iron.

【0004】一方、上記打ち抜き残材を、鋳鉄原料とす
ることをやめて、たとえば、軟鋼原料とすれば、溶解温
度が高い分、亜鉛が多く蒸発するので溶鋼に残留する亜
鉛は充分低下するが、ダスト処理や製鋼炉耐火物の寿命
低下という問題が惹起される。そのため、スクラップの
脱亜鉛に対して、特開平4−210434号に示される
ような化学的処理方法や、特開平4−346681号に
示されるような物理的方法が提案されている。
[0004] On the other hand, if the above punching residual material is replaced with a cast iron raw material and is, for example, a mild steel raw material, a large amount of zinc evaporates due to the high melting temperature, so that the zinc remaining in the molten steel is sufficiently reduced. This causes problems such as dust treatment and shortening of the life of refractories of steelmaking furnaces. Therefore, for dezincing scrap, a chemical treatment method as disclosed in JP-A-4-210434 and a physical method as disclosed in JP-A-4-346681 have been proposed.

【0005】[0005]

【発明が解決しようとする課題】ところが、上記提案さ
れている方法の場合、廃液の公害対策、設備費、脱亜鉛
効率、ランニングコスト、亜鉛回収率等において実用上
改善すべき点がある。
However, in the case of the above-proposed method, there are some points to be practically improved in measures against pollution of waste liquid, equipment cost, dezincification efficiency, running cost, zinc recovery rate and the like.

【0006】因に、高合金特殊鋼や活性元素を含む超合
金の溶解に用いられる所謂真空溶解炉では、脱亜鉛が完
全に実現できることは判っているが、設備費やランニン
グコスト、生産性等の面で鋳鉄鋳物の生産や鉄スクラッ
プの再生には実用的とはいえず、又、亜鉛の回収に関し
ては何らかの工夫がないと実用的ではない。
Incidentally, it is known that dezincification can be completely realized in a so-called vacuum melting furnace used for melting high alloy special steel and superalloy containing active elements, but equipment costs, running costs, productivity, etc. Therefore, it cannot be said that it is practical for the production of cast iron castings and the recycling of iron scrap, and it is not practical for the recovery of zinc without some measures.

【0007】そこで、本発明は、上述の分野における技
術的、経済的問題を解決し、昨今のエコロジー、エコマ
テリアルなどと称されるニーズに対応するために、亜鉛
の蒸発の温度と真空度、気相物質の凝縮についての知見
と研究に基づいてなされたもので、到達真空度を0.5
〜数kPa とした設備コストの比較的安価な真空溶解装置
を用いて、蒸発亜鉛を効率よく安全に回収できるような
蒸発亜鉛回収装置を提供しようとするものである。
Therefore, the present invention solves the technical and economic problems in the above-mentioned fields, and in order to meet the needs called the ecology and ecomaterials of the recent years, the temperature and vacuum degree of evaporation of zinc, It was made based on the knowledge and research on the condensation of gas phase substances, and the ultimate vacuum degree was 0.5.
The present invention aims to provide an evaporated zinc recovery device that can recover evaporated zinc efficiently and safely by using a vacuum melting device with a relatively low equipment cost of up to several kPa.

【0008】[0008]

【課題を解決するための手段】本発明は、上記課題を解
決するために、真空容器を構成する真空容器本体内に、
溶解炉を収容させて真空溶解装置を構成すると共に、上
記真空容器本体に着脱可能としてある真空容器蓋体内
に、上記溶解炉内の原料から蒸発した亜鉛を下面に蒸着
させ捕捉させるようにした円板を、昇降可能に且つ回転
可能に備え、更に、上記容器蓋体の内周面部に、上記円
板の回転により飛散させられた融解亜鉛を捕集するよう
にした捕集樋を設けた構成とする。
In order to solve the above-mentioned problems, the present invention provides a vacuum container main body which constitutes a vacuum container,
A vacuum melting device is configured to accommodate the melting furnace, and a vacuum container lid that is attachable to and detachable from the vacuum container body is formed by depositing zinc evaporated from the raw material in the melting furnace on the lower surface and capturing it. A structure in which a plate is rotatably and rotatably provided, and further, a collecting gutter is provided on an inner peripheral surface portion of the container lid body so as to collect the molten zinc scattered by the rotation of the disk. And

【0009】又、捕集樋を、容器蓋体の内周面部に設け
る代りに、円板の外周縁部内側に連設した構成としても
よい。
Further, instead of providing the collecting trough on the inner peripheral surface of the container lid, the collecting trough may be connected to the inside of the outer peripheral edge of the disc.

【0010】更に、真空容器に、不活性ガス導入管を接
続した構成とするとよい。
Further, it is preferable that an inert gas introducing pipe is connected to the vacuum container.

【0011】更に又、容器蓋体の内周面部に捕集樋を設
けた場合は、円板の直径を、溶解炉の内径の1.2〜
1.7倍とするのがよく、又、円板の外周縁に捕集樋を
連設した場合は、円板の直径を、溶解炉の内径の1.5
〜2.0倍とするのがよい。
Furthermore, in the case where a collecting trough is provided on the inner peripheral surface of the container lid, the diameter of the disk is 1.2 to the inner diameter of the melting furnace.
It is good to set 1.7 times, and when the collecting gutter is connected to the outer peripheral edge of the disk, make the diameter of the disk 1.5 times the inner diameter of the melting furnace.
It is better to set the value to 2.0 times.

【0012】[0012]

【作用】溶解炉内に原料を入れて円板を上方部に位置さ
せた状態において、真空減圧下で原料を加熱して行く
と、原料から亜鉛が蒸発させられて円板の下面に蒸着さ
せられる。しかる後、円板を下降させて溶解炉に近付け
ると共に回転させると、円板下面の蒸着亜鉛が溶解炉内
の溶銑の輻射熱により融解させられ、円板から受ける遠
心力で外方へ飛散させられる。飛散させられた亜鉛は容
器蓋体の内周面に衝突した後、流下して捕集樋にて捕集
される。
[Function] When the raw material is put in the melting furnace and the disc is positioned in the upper part, when the raw material is heated under reduced pressure in vacuum, zinc is evaporated from the raw material and deposited on the lower surface of the disc. To be Then, when the disk is lowered and brought closer to the melting furnace and rotated, the evaporated zinc on the lower surface of the disk is melted by the radiant heat of the hot metal in the melting furnace, and is scattered outward by the centrifugal force received from the disk. . The scattered zinc collides with the inner peripheral surface of the container lid, then flows down and is collected by a collecting trough.

【0013】一方、捕集樋を円板の外周縁部内側に連設
した場合には、融解亜鉛は遠心力により円板の外周部へ
寄せられて捕集樋にて受けられる。
On the other hand, when the collecting troughs are continuously provided inside the outer peripheral edge of the disc, the molten zinc is attracted to the outer peripheral portion of the disc by the centrifugal force and received by the collecting trough.

【0014】又、蒸着亜鉛を融解させて捕集するとき
に、真空容器内に不活性ガスを導入すると、亜鉛の一部
が再蒸発するのを防ぐことができる。
Further, when the vaporized zinc is melted and collected, if an inert gas is introduced into the vacuum container, it is possible to prevent part of the zinc from being re-evaporated.

【0015】更に、溶解炉の内径に対し、捕集樋を容器
蓋体の内周部に設けたときの円板の直径を1.2〜1.
7倍の範囲とし、捕集樋を円板の外周縁部に設けたとき
の円板の直径を1.5〜2.0倍の範囲とすると、それ
ぞれ蒸発亜鉛を円板の下面に効率よく蒸着させることが
できるようになる。
Further, with respect to the inner diameter of the melting furnace, the diameter of the disk when the collecting trough is provided on the inner peripheral portion of the container lid is 1.2 to 1.
If the diameter of the disk when the collecting gutter is provided on the outer peripheral edge of the disk is set to be 1.5 to 2.0 times, the evaporated zinc can be efficiently applied to the lower surface of the disk. It becomes possible to be vapor-deposited.

【0016】[0016]

【実施例】以下、本発明の実施例を図面を参照して説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0017】図1は本発明の一実施例を示すもので、上
端にフランジ部1aを有する所要深さの真空容器本体1
と、下端にフランジ部2aを有し上記真空容器本体1に
対して両フランジ部1a,2a間の真空シール3を境界
に着脱可能となるようにした所要高さの真空容器蓋体2
と、からなる非磁性体製の真空容器4を備え、且つ上記
真空容器本体1内に、印加電圧系を改造した低周波誘導
溶解炉あるいは高周波誘導溶解炉の如き誘導溶解炉5を
収容させ、更に、上記真空容器蓋体2の上側端部に、排
気系として、図示しない真空ポンプと接続した排気ダク
ト6を所要の傾斜配置として着脱可能に接続すると共
に、該排気ダクト6の途中に真空バルブ7を設置して、
到達真空度が0.5〜数kPa の簡易型の真空溶解装置8
を構成する。
FIG. 1 shows an embodiment of the present invention in which a vacuum container body 1 having a flange 1a at the upper end and having a required depth.
And a vacuum container lid 2 of a required height, which has a flange portion 2a at its lower end and is attachable to and detachable from the vacuum container body 1 with a vacuum seal 3 between both flange portions 1a and 2a as a boundary.
An induction melting furnace 5 such as a low frequency induction melting furnace or a high frequency induction melting furnace in which the applied voltage system is modified is housed in the vacuum container body 1. Further, as an exhaust system, an exhaust duct 6 connected to a vacuum pump (not shown) is detachably connected to the upper end of the vacuum container cover 2 in a required inclined arrangement, and a vacuum valve is provided in the middle of the exhaust duct 6. 7 is installed,
Simple vacuum melting device 8 with ultimate vacuum of 0.5 to several kPa
Make up.

【0018】上記真空容器4には、容器蓋体2の上端部
中心位置に、容器蓋体2上に設置した昇降駆動装置9及
び回転駆動装置10によって昇降及び回転駆動されるよ
うにした軸11を、真空シール兼回転軸受16を介して
上下方向に貫通させて配置し、且つ該軸11の下端に、
上記誘導溶解炉5の内径の1.2〜1.7倍の直径を有
する円板12の中心部を断熱材13を介して取り付け、
誘導溶解炉5の溶解原料あるいは溶銑から蒸発した亜鉛
を、上記円板12の下面に蒸着させて捕捉するようにす
ると共に、円板12の下面に捕捉した亜鉛を、溶銑の輻
射熱で融解させて円板12の回転による遠心力で外周へ
液滴として飛散させることができるようにする。
In the vacuum container 4, a shaft 11 is arranged at the center position of the upper end of the container lid 2 so as to be moved up and down and rotated by a lift drive device 9 and a rotation drive device 10 installed on the container cover 2. Is arranged so as to pass through in the vertical direction via the vacuum seal and rotary bearing 16, and at the lower end of the shaft 11,
The center portion of a disk 12 having a diameter 1.2 to 1.7 times the inner diameter of the induction melting furnace 5 is attached via a heat insulating material 13,
The molten raw material of the induction melting furnace 5 or zinc evaporated from the hot metal is vapor-deposited and captured on the lower surface of the disk 12, and the zinc captured on the lower surface of the disk 12 is melted by the radiant heat of the hot metal. The rotation of the disk 12 allows the droplets to be scattered to the outer periphery by centrifugal force.

【0019】又、上記真空容器4の容器蓋体2の下端内
周面部に、内方へ錐状に張り出させるようにした捕集樋
14を取り付け、上記円板12の回転で飛散させられた
亜鉛の液滴を捕集樋14にて受けられるようにし、且つ
上記容器蓋体2に、蒸着亜鉛融解飛散工程時に真空容器
4内へ不活性ガスを導入するための不活性ガス導入管1
5を、上記排気ダクト6を介して接続し、更に、上記排
気ダクト6の途中に、原料追加塔17を連設し、該原料
追加塔17から切り出した原料を、排気ダクト6の傾斜
に沿わせて落下させることにより誘導溶解炉5内に追加
供給させられるようにする。
Further, a collecting trough 14 which is formed so as to project inward in a conical shape is attached to the inner peripheral surface of the lower end of the container lid 2 of the vacuum container 4 and is scattered by the rotation of the disc 12. An inert gas introducing pipe 1 for allowing the zinc droplets to be received by the collecting trough 14 and for introducing an inert gas into the vacuum container 4 into the container lid 2 during the vapor deposition zinc melting and scattering process.
5 are connected via the exhaust duct 6, and a raw material addition tower 17 is connected in the middle of the exhaust duct 6, and the raw material cut out from the raw material addition tower 17 is guided along the slope of the exhaust duct 6. In addition, it is made to fall so that it can be additionally supplied into the induction melting furnace 5.

【0020】なお、円板12の回転数は200〜500
rpm に設定してある。又、容器蓋体2の高さは、円板1
2が最上部に位置しているときに溶銑の輻射熱によって
300〜350℃以下に保てるように設定してある。
The rotation speed of the disk 12 is 200 to 500.
It is set to rpm. Further, the height of the container lid 2 is the disc 1
When 2 is located at the top, it is set so as to be kept at 300 to 350 ° C. or lower by the radiant heat of the hot metal.

【0021】亜鉛メッキ鋼板スクラップを含む原料から
亜鉛の回収作業を行う場合は、予め、真空容器4の容器
蓋体2を容器本体1から取り外して近傍の所定位置に待
機させておいて、先ず、誘導溶解炉5内に原料を装入す
る。なお、上記容器蓋体2を待機させる場合、排気ダク
ト6からも切り離される。原料が装入されると、取り外
しておいた容器蓋体2を容器本体1に装着し、排気ダク
ト6を通して真空容器4内を真空排気(減圧)させる。
なお、このとき、円板12は最上部に位置させておく。
When recovering zinc from a raw material containing scraps of galvanized steel sheet, the container lid 2 of the vacuum container 4 is removed from the container body 1 in advance and left at a predetermined position in the vicinity thereof. Raw materials are charged into the induction melting furnace 5. When the container lid 2 is on standby, it is also disconnected from the exhaust duct 6. When the raw materials are charged, the removed container lid body 2 is attached to the container body 1, and the inside of the vacuum container 4 is evacuated (decompressed) through the exhaust duct 6.
At this time, the disk 12 is positioned at the top.

【0022】真空容器4内が所定の真空度になると、誘
導溶解炉5の通電を開始する。この誘導溶解炉5の通電
開始により、原料は赤熱する前の段階から徐々に蒸発し
始め、蒸発した亜鉛は上方の円板12の下面に蒸着して
行くことになる。誘導溶解炉5が加熱されてガス放出が
始まると、限られた排気能力では真空容器4内の真空度
は低下してしまうが、このとき、原料の温度が上昇して
いることから、すなわち、亜鉛の蒸気圧もどんどん高く
なることから、亜鉛の蒸発は続行される。
When the inside of the vacuum vessel 4 reaches a predetermined degree of vacuum, the induction melting furnace 5 is turned on. When the induction melting furnace 5 is energized, the raw material gradually begins to evaporate from the stage before it glows red, and the evaporated zinc is deposited on the lower surface of the upper disk 12. When the induction melting furnace 5 is heated and gas is released, the degree of vacuum in the vacuum container 4 decreases with a limited exhaust capacity, but at this time, since the temperature of the raw material rises, that is, Since the vapor pressure of zinc also increases, the evaporation of zinc continues.

【0023】上記誘導溶解炉5内の原料は加熱により溶
銑となるが、溶銑となる1300〜1400℃では10
数kPa の真空度でも脱亜鉛は充分進行するので、溶銑へ
の亜鉛の残留は数10ppm レベルとなる。この時点で、
排気ダクト6の真空バルブ7を閉じると共に、不活性ガ
ス導入管15により真空容器4内に不活性ガスを導入
し、更に、回転駆動装置10及び昇降駆動装置9の駆動
により、軸11の作動を介して円板12を溶銑からの輻
射で420〜500℃に加熱される位置まで回転させな
がら下降させる。なお、原料は誘導溶解炉5内で溶銑に
なると、レベルが下降するので、必要に応じ、原料追加
塔17より原料を切り出し、排気ダクト6の傾斜に沿わ
せて落下させることにより誘導溶解炉5内に追加供給す
るようにしておいてもよい。
The raw material in the induction melting furnace 5 becomes hot metal by heating, but it is 10 at 1300 to 1400 ° C., which is hot metal.
Since dezincification proceeds sufficiently even at a vacuum degree of several kPa, the amount of zinc remaining in the hot metal becomes several tens of ppm. at this point,
The vacuum valve 7 of the exhaust duct 6 is closed, an inert gas is introduced into the vacuum container 4 by the inert gas introduction pipe 15, and the rotation drive device 10 and the elevation drive device 9 are driven to operate the shaft 11. The disk 12 is rotated and lowered to a position where it is heated to 420 to 500 ° C. by the radiation from the hot metal. When the raw material becomes hot metal in the induction melting furnace 5, the level is lowered. Therefore, if necessary, the raw material is cut out from the raw material addition tower 17 and dropped along the inclination of the exhaust duct 6 to cause the induction melting furnace 5 to fall. You may make it additionally supply in.

【0024】上記の如く下降位置させられた円板12が
溶銑の輻射熱により420〜500℃に加熱されると、
円板12の下面に蒸着していた亜鉛が融解させられるこ
とになり、これが円板12の回転による遠心力で外周方
向へ向かって流れ、更に液滴(又はリン片状)となって
容器蓋体2の内周面へ向けて飛散させられ、衝突した
後、流下して捕集樋14内に捕集される。円板12を所
定時間回転させて亜鉛の捕集作業を終了すると、容器蓋
体2を容器本体1から取り外し、誘導溶解炉5内の溶銑
は成分調整されて出湯される。一方、円板12は冷却後
清掃され、更に、捕集樋14内の金属亜鉛は真空掃除器
等を用いて回収される。
When the disk 12 lowered as described above is heated to 420 to 500 ° C. by the radiant heat of the hot metal,
The zinc deposited on the lower surface of the disk 12 will be melted, and this will flow toward the outer peripheral direction due to the centrifugal force due to the rotation of the disk 12, and will further become droplets (or scaly pieces) to form a container lid. The particles are scattered toward the inner peripheral surface of the body 2, collide with each other, and then flow down to be collected in the collecting trough 14. When the disk 12 is rotated for a predetermined period of time to complete the zinc collecting operation, the container lid 2 is removed from the container body 1, and the molten pig iron in the induction melting furnace 5 is adjusted in composition and tapped. On the other hand, the disk 12 is cleaned after cooling and the metallic zinc in the collecting trough 14 is recovered by using a vacuum cleaner or the like.

【0025】上記において、円板12の直径が誘導溶解
炉5の内径、つまり溶湯面径の1.2〜1.7倍として
あるため、蒸発亜鉛を効率よく蒸着させることができる
と共に円滑に液滴として飛散させることができる。すな
わち、円板12の直径は溶湯面径の1.2倍以下である
と、亜鉛の蒸着量が少なく、1.7倍以上であると、回
転時に亜鉛が外周部に固着して部分的剥離が発生するこ
とにより回転バランスが崩れる虞がある。又、上記にお
いて、脱亜鉛終了後に蒸着亜鉛を融解させて飛散させる
とき、蒸気圧が高まって亜鉛の一部が再蒸発する虞があ
るが、その点本発明では、真空容器4内に不活性ガスを
導入して作業を進めるため、再蒸発を防ぐことができ
る。更に、上記においては、蒸発亜鉛の円板12の捕獲
量を増すつもりで最初から円板12を誘導溶解炉5に近
付けて配置することが考えられるが、その場合、輻射加
熱の影響で、逆に蒸発亜鉛が凝縮しなくなる問題があ
る。したがって、本発明では、脱亜鉛工程中のほとんど
の期間は円板12を最上部へ位置させるようにしてい
る。
In the above, since the diameter of the disk 12 is 1.2 to 1.7 times the inner diameter of the induction melting furnace 5, that is, the diameter of the surface of the molten metal, the evaporated zinc can be efficiently deposited and the liquid can be smoothly fed. Can be scattered as drops. That is, if the diameter of the disk 12 is 1.2 times or less of the molten metal surface diameter, the amount of zinc vapor deposition is small, and if it is 1.7 times or more, zinc adheres to the outer peripheral portion during rotation and is partially peeled. There is a possibility that the rotation balance may be lost due to the occurrence of the. Further, in the above, when vaporized zinc is melted and scattered after the completion of dezincification, the vapor pressure may increase and a part of zinc may be re-evaporated. Since gas is introduced to carry out the work, re-evaporation can be prevented. Further, in the above, it is conceivable to arrange the disk 12 close to the induction melting furnace 5 from the beginning in order to increase the capture amount of the evaporated zinc disk 12, but in that case, due to the effect of radiation heating, the reverse There is a problem that evaporated zinc does not condense. Therefore, in the present invention, the disc 12 is positioned at the top most of the time during the dezincification process.

【0026】次に、図2は本発明の他の実施例を示すも
ので、図1に示したと同様な構成としてある蒸発亜鉛回
収装置において、融解亜鉛を捕集するための捕集樋14
を、真空容器4の容器蓋体2の内周面部に設けることに
代えて、円板12の外周縁部に、錐状の導流壁18を介
して捕集樋14を連設し、該捕集樋14が円板12と一
体に昇降及び回転できるようにしたものである。上記円
板12の直径は誘導溶解炉5の内径の1.5〜2.0倍
に設定してある。なお、かかる実施例では、原料追加塔
17から切り出した原料を排気ダクト6の傾斜に沿わせ
て誘導溶解炉5内に追加供給する際に、原料供給経路が
捕集樋14の存在によって遮断されることがないよう
に、上記実施例のものよりも容器蓋体2の高さを高くし
て円板12が更に上方部まで移動できるように構成して
ある。
Next, FIG. 2 shows another embodiment of the present invention. A collecting trough 14 for collecting molten zinc in a vaporized zinc recovery apparatus having the same structure as shown in FIG.
Instead of being provided on the inner peripheral surface of the container lid 2 of the vacuum container 4, a collecting trough 14 is continuously provided on the outer peripheral edge of the disk 12 via a conical guiding wall 18. The collecting trough 14 is configured so that it can be raised and lowered and rotated integrally with the disc 12. The diameter of the disk 12 is set to 1.5 to 2.0 times the inner diameter of the induction melting furnace 5. In addition, in this embodiment, when the raw material cut out from the raw material addition tower 17 is additionally supplied into the induction melting furnace 5 along the inclination of the exhaust duct 6, the raw material supply path is blocked by the existence of the collection trough 14. Therefore, the height of the container lid 2 is made higher than that of the above-mentioned embodiment so that the disk 12 can move further up.

【0027】図2の実施例の場合には、円板12の下面
に蒸着した亜鉛が融解すると、円板12の回転による遠
心力で円板12の外周側へ流動させられ、導流壁18に
沿い流下させられるので、上記実施例の場合と同様に捕
集樋14にて亜鉛を捕集することができる。この際、円
板12の直径が誘導溶解炉5の内径の1.5〜2.0倍
としてあるため、蒸発亜鉛を効率よく蒸着させることが
できると共に設備的にも有利である。すなわち、円板1
2の直径が溶湯面径の1.5倍以下であると、捕集樋1
4の外側に亜鉛が蒸着してそれが飛散させられることで
回収が困難になるだけでなく、耐火物に侵入したりして
トラブルの発生原因になり、又、2.0倍以上である
と、容器蓋体2が不必要に大きくなるので排気系の容量
をアップさせねばならなくなってしまう。したがって、
円板12の直径を溶湯面径の1.5〜2.0倍の範囲と
することにより、亜鉛を捕集樋14の外側に付着させる
ことなく設備を大型化することもなく好適となる。
In the case of the embodiment shown in FIG. 2, when the zinc deposited on the lower surface of the disk 12 melts, it is caused to flow to the outer peripheral side of the disk 12 by the centrifugal force due to the rotation of the disk 12, and the flow guide wall 18 is formed. Since it is made to flow down along with, zinc can be collected by the collecting trough 14 as in the case of the above-mentioned embodiment. At this time, since the diameter of the disk 12 is 1.5 to 2.0 times the inner diameter of the induction melting furnace 5, evaporated zinc can be deposited efficiently and it is also advantageous in terms of equipment. That is, disk 1
If the diameter of 2 is less than 1.5 times the diameter of the molten metal surface, the collection trough 1
If zinc is vapor-deposited on the outside of 4 and scattered, it will not only be difficult to recover, but it will also enter into refractories and cause troubles, and if it is 2.0 times or more. Since the container lid body 2 becomes unnecessarily large, the capacity of the exhaust system must be increased. Therefore,
By setting the diameter of the disk 12 within the range of 1.5 to 2.0 times the diameter of the molten metal surface, it is suitable without adhering zinc to the outside of the collecting trough 14 and without increasing the size of the equipment.

【0028】なお、本発明は上記実施例のみに限定され
るものではなく、本発明の要旨を逸脱しない範囲内にお
いて種々変更を加え得ることは勿論である。
The present invention is not limited to the above-mentioned embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.

【0029】[0029]

【発明の効果】以上述べた如く、本発明の蒸発亜鉛回収
装置によれば、下記の如き種々の優れた効果を発揮す
る。 (1) 減圧溶解に近い排気能力の真空溶解装置の使用で済
むため、設備費が安価である。 (2) 亜鉛を蒸着させる円板には水冷装置を設ける必要が
ないので、水漏れによる爆発事故を発生させる必要がな
い。 (3) 溶湯となる前の段階で装入原料中の脱亜鉛がほとん
ど終了するので、溶湯突沸などの事故を発生させる虞が
ない。 (4) 回収される亜鉛は金属分に富んでいるので再利用資
源として有価である。 (5) 耐火物への亜鉛の侵入がないので、亜鉛メッキ鋼板
スクラップの使用割合を増やしても築炉回数が増えるこ
とはない。 (6) 既設の低周波や高周波誘導の大気溶解炉に対して
も、減圧下での放電を阻止するように印加電圧系統を改
造することで適用可能である。 (7) 脱亜鉛工程以外は大気溶解、鋳造の作業と同じであ
るので、良好な生産性が得られる。
As described above, the evaporated zinc recovery apparatus of the present invention exhibits various excellent effects as described below. (1) Equipment costs are low because a vacuum melting device with an exhaust capacity close to that of vacuum melting can be used. (2) Since it is not necessary to provide a water cooling device on the disk on which zinc is deposited, it is not necessary to cause an explosion accident due to water leakage. (3) Since dezincification in the charging raw material is almost completed before it becomes a molten metal, there is no risk of accident such as molten metal bumping. (4) Since the recovered zinc is rich in metals, it is valuable as a reusable resource. (5) Since there is no intrusion of zinc into the refractory, the number of furnace constructions will not increase even if the proportion of galvanized steel scrap used is increased. (6) It can be applied to existing low-frequency and high-frequency induction atmosphere melting furnaces by modifying the applied voltage system so as to prevent discharge under reduced pressure. (7) Other than the dezincification process, the work is the same as the work of melting in air and casting, so good productivity can be obtained.

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

【図1】本発明の蒸発亜鉛回収装置の一実施例を示す概
要図である。
FIG. 1 is a schematic diagram showing an embodiment of an evaporated zinc recovery device of the present invention.

【図2】本発明の他の実施例の概要図である。FIG. 2 is a schematic diagram of another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 真空容器本体 2 真空容器蓋体 4 真空容器 5 誘導溶解炉(溶解炉) 8 真空溶解装置 9 昇降駆動装置 10 回転駆動装置 11 軸 12 円板 14 捕集樋 15 不活性ガス導入管 DESCRIPTION OF SYMBOLS 1 Vacuum container main body 2 Vacuum container lid 4 Vacuum container 5 Induction melting furnace (melting furnace) 8 Vacuum melting device 9 Elevating drive device 10 Rotation drive device 11 Shaft 12 Disc 14 Collection gutter 15 Inert gas introduction pipe

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 真空容器を構成する真空容器本体内に、
溶解炉を収容させて真空溶解装置を構成すると共に、上
記真空容器本体に着脱可能としてある真空容器蓋体内
に、上記溶解炉内の原料から蒸発した亜鉛を下面に蒸着
させ捕捉させるようにした円板を、昇降可能に且つ回転
可能に備え、更に、上記容器蓋体の内周面部に、上記円
板の回転により飛散させられた融解亜鉛を捕集するよう
にした捕集樋を設けた構成を有することを特徴とする蒸
発亜鉛回収装置。
1. A vacuum container body constituting a vacuum container,
A vacuum melting apparatus is configured to accommodate a melting furnace, and a vacuum container lid that is detachably attached to the vacuum container body is provided with a circle for depositing zinc evaporated from the raw material in the melting furnace on the lower surface to capture it. A structure in which a plate is rotatably and rotatably provided, and further, a collecting gutter is provided on an inner peripheral surface portion of the container lid body so as to collect the molten zinc scattered by the rotation of the disk. An apparatus for recovering evaporated zinc, comprising:
【請求項2】 捕集樋を、容器蓋体の内周面部に設ける
代りに、円板の外周縁部内側に連設した請求項1記載の
蒸発亜鉛回収装置。
2. The evaporated zinc recovery apparatus according to claim 1, wherein the collection gutter is provided continuously inside the outer peripheral edge of the disk instead of being provided on the inner peripheral surface of the container lid.
【請求項3】 真空容器に、不活性ガス導入管を接続し
た請求項1又は2記載の蒸発亜鉛回収装置。
3. The evaporated zinc recovery apparatus according to claim 1, wherein an inert gas introducing pipe is connected to the vacuum container.
【請求項4】 円板の直径を、溶解炉の内径の1.2〜
1.7倍とした請求項1記載の蒸発亜鉛回収装置。
4. The diameter of the disk is 1.2 to the inner diameter of the melting furnace.
The evaporated zinc recovery apparatus according to claim 1, which is 1.7 times larger.
【請求項5】 円板の直径を、溶解炉の内径の1.5〜
2.0倍とした請求項2記載の蒸発亜鉛回収装置。
5. The diameter of the disk is 1.5 to the inner diameter of the melting furnace.
The evaporated zinc recovery apparatus according to claim 2, which is 2.0 times as large.
JP19883493A 1993-07-19 1993-07-19 Evaporated zinc recovery device Expired - Fee Related JP3319056B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19883493A JP3319056B2 (en) 1993-07-19 1993-07-19 Evaporated zinc recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19883493A JP3319056B2 (en) 1993-07-19 1993-07-19 Evaporated zinc recovery device

Publications (2)

Publication Number Publication Date
JPH0734149A true JPH0734149A (en) 1995-02-03
JP3319056B2 JP3319056B2 (en) 2002-08-26

Family

ID=16397696

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19883493A Expired - Fee Related JP3319056B2 (en) 1993-07-19 1993-07-19 Evaporated zinc recovery device

Country Status (1)

Country Link
JP (1) JP3319056B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101235762B1 (en) * 2010-12-28 2013-02-21 주식회사 포스코 Apparatus for recovering zinc metal from steel scrap and method thereof
CN103924087A (en) * 2014-04-02 2014-07-16 上海交通大学 Continuous vacuum separation recovery device of mixed metal of electronic waste
CN114034191A (en) * 2021-11-18 2022-02-11 湖南鑫泉科技有限公司 Device and method for detecting temperature of precision casting furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101235762B1 (en) * 2010-12-28 2013-02-21 주식회사 포스코 Apparatus for recovering zinc metal from steel scrap and method thereof
CN103924087A (en) * 2014-04-02 2014-07-16 上海交通大学 Continuous vacuum separation recovery device of mixed metal of electronic waste
CN103924087B (en) * 2014-04-02 2016-05-18 上海交通大学 The continuous separating and reclaiming device of vacuum of electron wastes hybrid metal
CN114034191A (en) * 2021-11-18 2022-02-11 湖南鑫泉科技有限公司 Device and method for detecting temperature of precision casting furnace
CN114034191B (en) * 2021-11-18 2023-11-24 湖南鑫泉科技有限公司 Device and method for detecting furnace temperature of precision casting furnace

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