JP2011042851A - Dezincification apparatus - Google Patents

Dezincification apparatus Download PDF

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Publication number
JP2011042851A
JP2011042851A JP2009192989A JP2009192989A JP2011042851A JP 2011042851 A JP2011042851 A JP 2011042851A JP 2009192989 A JP2009192989 A JP 2009192989A JP 2009192989 A JP2009192989 A JP 2009192989A JP 2011042851 A JP2011042851 A JP 2011042851A
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heating
chamber
tank
heating chamber
preheating
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Shigeyuki Nakamura
茂之 中村
Toshimitsu Fujiwara
利光 藤原
Naotaka Tanahashi
尚貴 棚橋
Takahiro Yamada
高裕 山田
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Chubu Electric Power Co Inc
Tokuden Co Ltd Hyogo
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Chubu Electric Power Co Inc
Tokushu Denkyoku Co Ltd
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Application filed by Chubu Electric Power Co Inc, Tokushu Denkyoku Co Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP2009192989A priority Critical patent/JP2011042851A/en
Priority to EP20090839046 priority patent/EP2319946B1/en
Priority to PCT/JP2009/006785 priority patent/WO2011024244A1/en
Priority to US12/833,412 priority patent/US20110042371A1/en
Publication of JP2011042851A publication Critical patent/JP2011042851A/en
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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)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a dezincification apparatus which can surely remove zinc. <P>SOLUTION: This dezincification apparatus includes: a preheating tank 10 which is provided with an input port for charging a zinc-plated scrap steel sheet and with a preheating chamber 12 for subjecting the charged scrap steel sheet to preliminary heating; a preheat tank 20 which is arranged in the lower part of the preheating tank 10 and is provided with a preheat chamber 22 that makes a heating coil 23 for preheating the preliminary heated scrap steel sheet wind around its outer circumference; a heating tank 30 which is arranged in the lower part of the preheat tank 20 and is provided with a heating chamber 32 that makes a heating coil 33 for fully heating a preheated scrap steel sheet wind around its outer circumference; a residual heat tank 40 which is arranged in the lower part of the heating tank 30 and is provided with a residual heat chamber 41 for staying the fully heated scrap steel sheet therein; dampers 13, 24 and 34 which seal and section each tank and also drop and transfer the scrap steel sheet to the heating chamber which is located in the next lower part; and an exhaust pipe 50 which is connected to the preheat tank 20, the heating tank 30 and the residual heat tank 40. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、亜鉛メッキ鋼板を加熱して亜鉛を蒸発させて除去する誘導加熱方式の脱亜鉛装置に関する。   The present invention relates to an induction heating type dezincing apparatus that heats a galvanized steel sheet to evaporate and remove zinc.

従来、鋳物業界においては、スクラップ鋼板を溶解して鋳鉄の原材料とする割合が増えており、再利用されるスクラップ鋼板の代表的なものに亜鉛メッキ鋼板がある。スクラップ鋼板の溶解手段としては電気炉溶解法が常用されているが、これにより亜鉛メッキ鋼板を溶解する場合には種々の問題がある。例えば、亜鉛メッキ鋼板をそのまま溶解すると、亜鉛が炉の耐火物を浸透通過して加熱コイルを損傷させ、溶解設備の寿命を縮めることになって保全費を増加させてしまう。また、亜鉛は沸点が低くて蒸発しやすく、亜鉛蒸気による作業環境の悪化を招いたり、亜鉛が製品に混入されて品質を劣化させてしまったりすることもある。   2. Description of the Related Art Conventionally, in the casting industry, the proportion of scrap steel plates that are melted into raw materials for cast iron has increased, and galvanized steel plates are typical of scrap steel plates that are reused. An electric furnace melting method is commonly used as a means for melting scrap steel plates, but there are various problems when melting galvanized steel plates. For example, if a galvanized steel sheet is melted as it is, zinc penetrates and passes through the furnace refractory, damages the heating coil, shortens the life of the melting equipment, and increases maintenance costs. In addition, zinc has a low boiling point and easily evaporates, which may lead to deterioration of the working environment due to zinc vapor, and may deteriorate the quality due to zinc being mixed into the product.

このような問題に対して、特許文献1に示されるような誘導加熱式脱亜鉛装置が提案されている。この誘導加熱式脱亜鉛装置によれば、加熱コイルに通電して亜鉛メッキ鋼板を誘導加熱して亜鉛を溶融させるとともに、溶融した亜鉛の一部が蒸発して生じる亜鉛華を材料排出口から外部に排気することができる。   In response to such a problem, an induction heating type dezincing apparatus as shown in Patent Document 1 has been proposed. According to this induction heating type dezincing apparatus, the zinc coil is melted by energizing the heating coil by inductively heating the galvanized steel sheet, and the zinc white produced by evaporation of a part of the molten zinc is externally discharged from the material discharge port. Can be exhausted.

特開平8−83676号公報JP-A-8-83676

しかしながら、上記特許文献1の装置では、加熱筒の中央部分に位置する亜鉛メッキ鋼板にまでは熱が行きわたりにくい等、均一な温度での加熱が困難であり、亜鉛の除去が不十分かつ亜鉛が酸化された状態で誘導溶解炉に搬送され、亜鉛が製品に混入してしまうおそれがある。また、誘導溶解炉内において湯面に酸化亜鉛を含むノロが多量に発生し、周囲の耐火物を溶損させたり、耐火物にノロが取り込まれてZnO・SiO混合酸化物が耐火物表面に付着して盛り上がり、材料投入時に材料が棚つり状態となって、先に投入された下方部の材料の異常加熱を引き起こしたりするおそれもある。 However, in the apparatus of Patent Document 1, it is difficult to heat the galvanized steel sheet located at the center portion of the heating cylinder, for example, it is difficult to heat at a uniform temperature. There is a possibility that zinc is conveyed to the induction melting furnace in an oxidized state and zinc is mixed into the product. In addition, a large amount of zinc oxide containing zinc oxide is generated on the molten metal surface in the induction melting furnace, the surrounding refractory is melted down, or noro is taken into the refractory, and the ZnO / SiO 2 mixed oxide becomes the refractory surface. There is also a possibility that the material will rise and stick to the surface, and when the material is charged, the material will be in a suspended state, causing abnormal heating of the material in the lower portion that has been previously charged.

そこで、本発明は、上記課題に鑑みなされたものであり、確実な亜鉛の除去を可能とする脱亜鉛装置を提供することを目的とする。また、亜鉛蒸気を確実に排出することができる脱亜鉛装置を提供することをも目的とする。   Then, this invention is made | formed in view of the said subject, and it aims at providing the dezincing apparatus which enables the reliable removal of zinc. Another object of the present invention is to provide a dezincing apparatus that can reliably discharge zinc vapor.

上記の課題を解決するため、本発明に係る脱亜鉛装置は、亜鉛メッキ鋼板に熱を加えるための第一加熱室と、前記第一加熱室の下方に位置し、前記第一加熱室における加熱が施された亜鉛メッキ鋼板に前記第一加熱室における加熱よりも高い温度の熱を加えるための空間を有する第二加熱室と、前記第一加熱室と前記第二加熱室とを密閉して区画するとともに、第一加熱室から第二加熱室へ亜鉛メッキ鋼板を落下移動させる開閉手段と、第一加熱室及び第二加熱室の外周に巻回され、前記第一加熱室及び前記第二加熱室において亜鉛メッキ鋼板に加熱を施すための加熱コイルとを備えることを特徴とする。   In order to solve the above problems, a dezincing apparatus according to the present invention includes a first heating chamber for applying heat to a galvanized steel sheet, and a heating in the first heating chamber, which is located below the first heating chamber. A second heating chamber having a space for applying heat at a temperature higher than that of heating in the first heating chamber to the galvanized steel sheet to which is applied, and sealing the first heating chamber and the second heating chamber Opening and closing means for partitioning and moving the galvanized steel sheet from the first heating chamber to the second heating chamber, wound around the outer periphery of the first heating chamber and the second heating chamber, the first heating chamber and the second heating chamber A heating coil for heating the galvanized steel sheet in the heating chamber is provided.

これにより、亜鉛メッキがなされたスクラップ鋼板に複数の加熱室で段階的に熱を加えるとともに、各加熱室を落下移動させる度に攪拌することにより、スクラップ鋼板に均一な熱を加えることができるので、効率よく確実に亜鉛を除去することができる脱亜鉛装置が実現される。   As a result, the galvanized scrap steel plate can be heated in stages in a plurality of heating chambers, and by stirring each time the heating chambers are dropped and moved, uniform heat can be applied to the scrap steel plates. Thus, a dezincing apparatus that can efficiently and reliably remove zinc is realized.

ここで、前記脱亜鉛装置は、さらに、前記第一加熱室の上方に位置し、亜鉛メッキ鋼板を投入するための投入口を有し、投入された亜鉛メッキ鋼板に前記第一加熱室における加熱よりも低い温度の熱を加えるための空間を有する予備加熱室を備え、前記開閉手段は、前記予備加熱室と前記第一加熱室とを密閉して区画するとともに、予備加熱室から第一加熱室へ亜鉛メッキ鋼板を落下移動させるのが好ましい。   Here, the dezincing device is further located above the first heating chamber, and has a charging port for charging a galvanized steel sheet, and the galvanized steel sheet is heated in the first heating chamber. A preheating chamber having a space for applying heat at a lower temperature, and the opening / closing means hermetically partitions the preheating chamber and the first heating chamber, and the first heating from the preheating chamber It is preferable to drop and move the galvanized steel sheet to the chamber.

これにより、さらに多段的な加熱および落下で、スクラップ鋼板を攪拌し、均一な加熱ができるようになる。   Thereby, the scrap steel plate can be stirred and heated evenly by multi-stage heating and dropping.

また、前記脱亜鉛装置は、さらに、前記第二加熱室の下方に位置し、前記第二加熱室における加熱が施された亜鉛メッキ鋼板を滞留させる余熱室を備えるのが好ましい。   Moreover, it is preferable that the said dezincification apparatus is further provided with the preheating chamber which is located under the said 2nd heating chamber and retains the galvanized steel plate with which the heating in the said 2nd heating chamber was given.

これにより、複数回の加熱で帯びた余熱によってスクラップ鋼板に残存する亜鉛成分も確実に除去することができる。   Thereby, the zinc component remaining on the scrap steel plate due to the residual heat generated by the heating a plurality of times can be reliably removed.

また、前記脱亜鉛装置は、さらに、第一加熱室及び第二加熱室に接続された排気パイプを備えるとするのが好ましい。なお、前記排気パイプの下流側には、亜鉛成分の捕集フィルタ、誘引ファン並びに必要に応じて冷却器が接続され、亜鉛を捕捉後、排気される。   Further, it is preferable that the dezincing device further includes an exhaust pipe connected to the first heating chamber and the second heating chamber. A zinc component collecting filter, an induction fan, and a cooler as necessary are connected to the downstream side of the exhaust pipe, and after exhausting the zinc, the exhaust pipe is exhausted.

これにより、密閉された各加熱室から亜鉛蒸気を排気パイプにより吸引して排出するので、亜鉛蒸気が外部へ漏れ出すことがなく、確実な亜鉛蒸気の排出を可能とする脱亜鉛装置が実現される。   As a result, zinc vapor is sucked and discharged from each sealed heating chamber through the exhaust pipe, so that a zinc removal device that can reliably discharge zinc vapor is realized without leakage of zinc vapor to the outside. The

このように、本発明に係る脱亜鉛装置によれば、複数の加熱室に区画してスクラップ鋼板を各加熱室へ落下移動させ、各加熱室においてスクラップ鋼板を攪拌するとともに各加熱室内でのスクラップ鋼板の充填位置が変化するので、スクラップ鋼板へのより均一な加熱が可能となり、確実な亜鉛除去を実現することができる。また、スクラップ鋼板を落下移動させる開閉装置が、各加熱室を密閉しているので、亜鉛蒸気が外に漏れることなく、亜鉛蒸気の排出路となる排気パイプへ誘導することができ、亜鉛蒸気の確実な排気も可能となる。   As described above, according to the dezincing apparatus according to the present invention, the scrap steel plates are divided into a plurality of heating chambers, and the scrap steel plates are dropped and moved to the respective heating chambers, and the scrap steel plates are stirred in the respective heating chambers. Since the filling position of the steel plate changes, the scrap steel plate can be heated more uniformly, and reliable zinc removal can be realized. In addition, since the opening and closing device that moves the scrap steel plate in a closed manner closes each heating chamber, the zinc vapor can be guided to the exhaust pipe that becomes the discharge path of the zinc vapor without leaking outside. Reliable exhaust is also possible.

脱亜鉛装置の概略を示す図である。It is a figure which shows the outline of a dezincification apparatus. 脱亜鉛装置の別構成の概略を示す図である。It is a figure which shows the outline of another structure of a dezincification apparatus.

以下、本発明に係る脱亜鉛装置について図を参照しながら説明する。   Hereinafter, a dezincing apparatus according to the present invention will be described with reference to the drawings.

図1は、脱亜鉛装置の概略を示す図である。   FIG. 1 is a diagram showing an outline of a dezincing apparatus.

脱亜鉛装置1は、亜鉛メッキ鋼板を加熱して亜鉛を蒸発させる誘導加熱式の脱亜鉛炉であり、予備加熱槽10、予熱槽20、加熱槽30、余熱槽40および排気パイプ50を備えている。   The dezincing apparatus 1 is an induction heating type dezincification furnace that heats a galvanized steel sheet to evaporate zinc, and includes a preheating tank 10, a preheating tank 20, a heating tank 30, a residual heat tank 40, and an exhaust pipe 50. Yes.

予備加熱槽10は、上部にスクラップ鋼板を投入するための投入口を備えており、装置内に投入されたスクラップ鋼板を貯留するための貯留室11と、スクラップ鋼板に予備加熱を施すための予備加熱室12と、予備加熱槽10と予熱槽20とを区画する開閉装置として観音開き式のダンパ13とを備えている。予備加熱室12における予備加熱は、その下方に位置する予熱槽20から伝わる500℃以下の温度の熱による加熱であり、この加熱によりスクラップ鋼板に含まれる水分や油分などが除去される。   The preheating tank 10 is provided with an inlet for charging a scrap steel plate in the upper part, a storage chamber 11 for storing the scrap steel plate charged in the apparatus, and a reserve for preheating the scrap steel plate. A double door type damper 13 is provided as an opening / closing device that partitions the heating chamber 12 and the preheating tank 10 and the preheating tank 20. The preheating in the preheating chamber 12 is heating by the heat of the temperature of 500 degrees C or less transmitted from the preheating tank 20 located in the lower part, The water | moisture content, oil content, etc. which are contained in a scrap steel plate are removed by this heating.

予熱槽20は、予備加熱室12で予備加熱がされた後のスクラップ鋼板を加熱するための空間を有する槽であり、ダンパ13を開くことにより送り込まれるスクラップ鋼板を貯留するための貯留室21と、スクラップ鋼板に予熱を加えるための予熱室22と、予熱室22の外周に巻回された加熱コイル23と、予熱槽20と加熱槽30とを区画する観音開き式のダンパ24とを備えている。加熱コイル23は、誘導加熱電源(図示せず)に接続されており、誘導加熱電源からの通電によって、予熱室22内のスクラップ鋼板を誘導加熱する。予熱室22における予熱は、この加熱コイル23による500〜900℃の温度の熱による1回目の加熱である。この加熱によりスクラップ鋼板の亜鉛メッキは溶融し、その一部は蒸発して亜鉛蒸気となって除去されるとともに、その熱は上方に位置する予備加熱室12へ伝わって予備加熱としても利用される。なお、予熱槽20内の雰囲気は、空気雰囲気でもよいが、亜鉛の酸化を防いで亜鉛の蒸発を促進させるために、窒素やアルゴン等を流入させた不活性雰囲気もしくは一酸化炭素等を含む還元雰囲気とするのがよい。   The preheating tank 20 is a tank having a space for heating the scrap steel plate after being preheated in the preheating chamber 12, and a storage chamber 21 for storing the scrap steel plate fed by opening the damper 13. A preheating chamber 22 for preheating the scrap steel plate, a heating coil 23 wound around the outer periphery of the preheating chamber 22, and a double-spread damper 24 that partitions the preheating tank 20 and the heating tank 30 are provided. . The heating coil 23 is connected to an induction heating power source (not shown), and induction heats the scrap steel plate in the preheating chamber 22 by energization from the induction heating power source. The preheating in the preheating chamber 22 is the first heating by the heating coil 23 at a temperature of 500 to 900 ° C. By this heating, the zinc plating of the scrap steel plate is melted and a part thereof is evaporated and removed as zinc vapor, and the heat is transferred to the preheating chamber 12 located above and used as preheating. . The atmosphere in the preheating tank 20 may be an air atmosphere, but in order to prevent the oxidation of zinc and promote the evaporation of zinc, a reduction containing an inert atmosphere or carbon monoxide into which nitrogen, argon or the like is introduced. The atmosphere should be good.

加熱槽30は、予熱室22で予熱が加えられた後のスクラップ鋼板を加熱するための空間を有する槽であり、ダンパ24を開くことにより送り込まれるスクラップ鋼板を貯留するための貯留室31と、スクラップ鋼板に本加熱を加えるための加熱室32と、加熱室32の外周に巻回された加熱コイル33と、加熱槽30と余熱槽40とを区画する観音開き式のダンパ34とを備えている。加熱コイル33は、加熱コイル22と同様に、誘導加熱電源からの通電によって、加熱室32内のスクラップ鋼板を誘導加熱する。加熱室32における本加熱は、この加熱コイル33による900〜1100℃の温度の熱による2回目の加熱である。この加熱により予熱室22で除去しきれなかったスクラップ鋼板の亜鉛メッキは溶融、蒸発して亜鉛蒸気となって除去される。なお、加熱槽30内の雰囲気も、空気雰囲気としてもよいが、亜鉛の酸化を防いで亜鉛の蒸発を促進させるために、窒素やアルゴン等を流入させた不活性雰囲気もしくは一酸化炭素等を含む還元雰囲気とするのがよい。   The heating tank 30 is a tank having a space for heating the scrap steel plate after preheating is applied in the preheating chamber 22, and a storage chamber 31 for storing the scrap steel plate fed by opening the damper 24; A heating chamber 32 for applying main heating to the scrap steel plate, a heating coil 33 wound around the outer periphery of the heating chamber 32, and a double door damper 34 that partitions the heating tank 30 and the preheating tank 40 are provided. . Similar to the heating coil 22, the heating coil 33 induction heats the scrap steel plate in the heating chamber 32 by energization from an induction heating power source. The main heating in the heating chamber 32 is the second heating by heat at a temperature of 900 to 1100 ° C. by the heating coil 33. The zinc plating of the scrap steel plate that could not be removed in the preheating chamber 22 by this heating is melted and evaporated to be removed as zinc vapor. The atmosphere in the heating tank 30 may be an air atmosphere, but includes an inert atmosphere or carbon monoxide into which nitrogen, argon, or the like is introduced in order to prevent zinc oxidation and promote zinc evaporation. A reducing atmosphere is preferable.

余熱槽40は、加熱室32で本加熱が加えられたスクラップ鋼板を、その余熱によって亜鉛を除去するとともに、装置の駆動部が高温で損傷することを抑制すべく冷却するための空間を有する槽であり、ダンパ34を開くことにより送り込まれるスクラップ鋼板を貯留し、スクラップ鋼板の余熱を利用して残存する亜鉛成分を除去するための余熱室41と、亜鉛が除去されたスクラップ鋼板を装置外へ排出する排出部42とを備えている。   The residual heat tank 40 is a tank having a space for cooling the scrap steel plate subjected to the main heating in the heating chamber 32 to remove zinc by the residual heat and to prevent the drive unit of the apparatus from being damaged at a high temperature. The scrap steel plate sent by opening the damper 34 is stored, the residual heat chamber 41 for removing the remaining zinc component using the residual heat of the scrap steel plate, and the scrap steel plate from which the zinc has been removed are out of the apparatus. And a discharge portion 42 for discharging.

排気パイプ50は、パイプ内を吸気して亜鉛蒸気を外部へ排出するための配管であり、予熱槽20、加熱槽30及び余熱槽40に接続されて、これらの各槽で発生する亜鉛蒸気の排出路として機能する。なお、排気パイプ50の下流側には、亜鉛成分の捕集フィルタ、誘引ファン並びに必要に応じて冷却器が接続され、亜鉛を捕捉した後に外部へ排出するようになっている。   The exhaust pipe 50 is a pipe for sucking the inside of the pipe and discharging the zinc vapor to the outside. The exhaust pipe 50 is connected to the preheating tank 20, the heating tank 30, and the residual heat tank 40, and the zinc vapor generated in each of these tanks. Functions as a discharge channel. A zinc component collecting filter, an attracting fan, and a cooler as necessary are connected to the downstream side of the exhaust pipe 50 so that zinc is captured and discharged to the outside.

このように構成される脱亜鉛装置1におけるスクラップ鋼板の脱亜鉛処理手順は、次のようになる。   The dezincing procedure of the scrap steel plate in the dezincing apparatus 1 configured as described above is as follows.

予備加熱槽10へ投入されたスクラップ鋼板は貯留室11に滞留する。先に投入されたスクラップ鋼板が予熱槽20に送り込まれると、貯留室11のスクラップ鋼板は予備加熱室12へと順次落下していく。予備加熱室12で予備加熱が施されたスクラップ鋼板は、水分や油分などが除去され、ダンパ13の開放により予熱槽20へ送り込まれる。除去された水分や油分などは、水蒸気等となって排気パイプ50を通じて外部へ排出される。   The scrap steel plate charged into the preheating tank 10 stays in the storage chamber 11. When the previously introduced scrap steel plate is fed into the preheating tank 20, the scrap steel plate in the storage chamber 11 sequentially falls into the preheating chamber 12. The scrap steel plate that has been preheated in the preheating chamber 12 is freed of moisture, oil, and the like, and is sent to the preheating tank 20 by opening the damper 13. The removed moisture, oil, and the like become steam and the like and are discharged to the outside through the exhaust pipe 50.

予熱槽20へ送り込まれたスクラップ鋼板は貯留室21に滞留する。ここでも、先に投入されたスクラップ鋼板が加熱槽30へ移動すると貯留室21のスクラップ鋼板は予熱室22へと順次落下する。スクラップ鋼板が落下移動することにより攪拌されるので、室内のスクラップ鋼板には均一に熱が加えられることとなる。予熱室22で予熱が施されたスクラップ鋼板は、亜鉛が除去され、ダンパ24の開放により加熱槽30へ送り込まれる。予熱室22における予熱で除去される亜鉛は、亜鉛蒸気となって排気パイプ50を通じて外部へ排出される。このとき、ダンパ13によって予熱槽20と予備加熱槽10とは密閉されているので、亜鉛蒸気が外に漏れにくくなっている。   The scrap steel plate sent to the preheating tank 20 stays in the storage chamber 21. Here again, when the previously introduced scrap steel plate moves to the heating tank 30, the scrap steel plate in the storage chamber 21 falls sequentially into the preheating chamber 22. Since the scrap steel plate is agitated by falling and moving, heat is uniformly applied to the indoor scrap steel plate. Zinc is removed from the scrap steel plate preheated in the preheating chamber 22, and the steel plate is fed into the heating tank 30 by opening the damper 24. Zinc removed by preheating in the preheating chamber 22 becomes zinc vapor and is discharged to the outside through the exhaust pipe 50. At this time, since the preheating tank 20 and the preheating tank 10 are hermetically sealed by the damper 13, the zinc vapor is difficult to leak outside.

続いて、加熱槽30へ送り込まれたスクラップ鋼板は貯留室31に滞留する。同様に、先に投入されたスクラップ鋼板が余熱槽40へ移動すると貯留室31のスクラップ鋼板は加熱室32へと順次落下し、その際に攪拌される。この攪拌によって予熱室22で亜鉛を除去しきれなかったスクラップ鋼板も、加熱室32における本加熱により亜鉛が除去されることになる。亜鉛が除去されたスクラップ鋼板は、ダンパ34の開放により余熱槽40へ送り込まれ、除去された亜鉛は亜鉛蒸気となって排気パイプ50を介して排出される。このとき、ダンパ24が加熱槽30と予熱槽20とを密閉し、亜鉛蒸気を外に漏出しないようにしている。   Subsequently, the scrap steel plate sent to the heating tank 30 stays in the storage chamber 31. Similarly, when the previously thrown-in scrap steel plate moves to the preheating tank 40, the scrap steel plate in the storage chamber 31 sequentially falls into the heating chamber 32 and is stirred at that time. The scrap steel plate that has not been able to remove the zinc in the preheating chamber 22 by this stirring is also removed by the main heating in the heating chamber 32. The scrap steel plate from which zinc has been removed is sent to the residual heat tank 40 by opening the damper 34, and the removed zinc is discharged through the exhaust pipe 50 as zinc vapor. At this time, the damper 24 seals the heating tank 30 and the preheating tank 20 so that zinc vapor does not leak out.

スクラップ鋼板は、余熱槽40へ送り込まれると余熱室41に滞留し、加熱室32における本加熱で帯びた余熱によって残りの亜鉛成分が除去される。余熱槽40への落下移動によりスクラップ鋼板は攪拌されて均一に余熱が加えられるので、残存する亜鉛成分を亜鉛蒸気として確実に除去することができる。ダンパ34が余熱槽40と加熱槽30とを密閉しているので、亜鉛蒸気は排気パイプ50から排出され、外へ漏れ出ることがない。余熱室41で所定時間滞留した後、亜鉛が除去されたスクラップ鋼板は、プッシャー等によって押し出されて排出部42から外へ排出される。   When the scrap steel plate is fed into the preheating tank 40, the scrap steel plate stays in the preheating chamber 41, and the remaining zinc component is removed by the residual heat generated by the main heating in the heating chamber 32. The scrap steel plate is agitated by the drop movement to the residual heat tank 40 and the residual heat is uniformly applied, so that the remaining zinc component can be reliably removed as zinc vapor. Since the damper 34 seals the residual heat tank 40 and the heating tank 30, the zinc vapor is discharged from the exhaust pipe 50 and does not leak outside. After staying in the residual heat chamber 41 for a predetermined time, the scrap steel plate from which zinc has been removed is pushed out by a pusher or the like and discharged from the discharge portion 42 to the outside.

以上説明したように、本実施の形態に係る脱亜鉛装置によれば、スクラップ鋼板を加熱する空間を複数に区画して加熱するバッチ連続式としているから、脱亜鉛効率に優れた装置を実現できる。また、スクラップ鋼板を落下移動させるので、各加熱空間においてスクラップ鋼板が攪拌される。この攪拌効果によりスクラップ鋼板へ均一な加熱が可能となるので、確実な亜鉛除去が実現可能となる。さらに、スクラップ鋼板を落下移動させる開閉装置が、各加熱空間を密閉して区画するので、亜鉛蒸気は外に漏れ出ることなく、側方に設置された排気パイプから排出され、確実な亜鉛蒸気の排気を可能としている。   As described above, according to the dezincing apparatus according to the present embodiment, a batch continuous system that heats by dividing a space for heating a scrap steel plate into a plurality of parts can be realized, and thus an apparatus having excellent dezincing efficiency can be realized. . Moreover, since the scrap steel plate is dropped and moved, the scrap steel plate is stirred in each heating space. This stirring effect makes it possible to heat the scrap steel plate uniformly, so that reliable zinc removal can be realized. In addition, since the opening and closing device that moves the scrap steel plate in a sealed manner separates each heating space, zinc vapor is discharged from the exhaust pipe installed on the side without leaking outside, and reliable zinc vapor Exhaust is possible.

以上、本発明に係る脱亜鉛装置について、実施の形態に基づいて説明したが本発明はこれに限定されるものではなく、本発明の目的を達成でき、かつ発明の要旨を逸脱しない範囲内で種々設計変更が可能であり、それらも全て本発明の範囲内に包含されるものである。   As mentioned above, although the dezincing apparatus based on this invention was demonstrated based on embodiment, this invention is not limited to this, In the range which can achieve the objective of this invention and does not deviate from the summary of invention. Various design changes are possible and all are included within the scope of the present invention.

例えば、上記実施の形態では、開閉手段として観音開き式のダンパを用いたが、各槽を区画して密閉するものであればスライド式の扉などその他の開閉手段を用いてもよい。   For example, in the above-described embodiment, a double door type damper is used as the opening / closing means, but other opening / closing means such as a sliding door may be used as long as each tank is partitioned and sealed.

また、予熱槽の外周と加熱槽の外周とに巻き回される加熱コイルがそれぞれ別の誘導加熱電源に接続されているとしてもよいし、一つの誘導加熱電源に接続された加熱コイルを両槽の外周に巻き回すとしてもよい。上記実施の形態で示すように、予熱槽の外周に巻き回される加熱コイルと加熱槽の外周に巻き回される加熱コイルとを分けることにより、加熱温度の調整が槽ごとに可能となる。   Further, the heating coils wound around the outer periphery of the preheating tank and the outer periphery of the heating tank may be connected to different induction heating power sources, or the heating coils connected to one induction heating power source may be connected to both tanks. It is good also as winding around the outer periphery. As shown in the above embodiment, by dividing the heating coil wound around the preheating tank and the heating coil wound around the heating tank, the heating temperature can be adjusted for each tank.

さらに、予備加熱では下方に位置する予熱槽から伝わる熱を用いるとしていることから、図2に示すように、予備加熱槽と予熱槽とを区画密閉せずに一体化して、予熱槽で予備加熱と予熱とを施す構成の脱亜鉛装置2としてもよい。その一方、予備加熱において予熱槽からの熱を用いるのではなく、予備加熱室の外周に加熱コイルを巻回すことによって熱を加えることとしてもよい。   Furthermore, since preheating uses heat transmitted from the lower preheating tank, as shown in FIG. 2, the preheating tank and the preheating tank are integrated without being hermetically sealed and preheated in the preheating tank. It is good also as the dezincification apparatus 2 of the structure which performs preheating. On the other hand, instead of using the heat from the preheating tank in the preheating, heat may be applied by winding a heating coil around the outer periphery of the preheating chamber.

本発明に係る脱亜鉛装置は、亜鉛メッキがされたスクラップ鋼板の亜鉛除去装置として好適である。   The dezincing apparatus according to the present invention is suitable as a zinc removing apparatus for scrap steel sheets plated with zinc.

1、2 脱亜鉛装置
10 予備加熱槽
11、11a、21、21a、31 貯留室
12、12a 予備加熱室
13、24、34 ダンパ
20、20a 予熱槽
22 予熱室
23、33 加熱コイル
30 加熱槽
32 加熱室
40 余熱槽
41 余熱室
42 排出部
50 排気パイプ
DESCRIPTION OF SYMBOLS 1, 2 Dezincification apparatus 10 Preheating tank 11, 11a, 21, 21a, 31 Storage chamber 12, 12a Preheating chamber 13, 24, 34 Damper 20, 20a Preheating tank 22 Preheating chamber 23, 33 Heating coil 30 Heating tank 32 Heating chamber 40 Heating tank 41 Heating chamber 42 Discharge part 50 Exhaust pipe

Claims (4)

亜鉛メッキ鋼板に熱を加えるための第一加熱室と、
前記第一加熱室の下方に位置し、前記第一加熱室における加熱が施された亜鉛メッキ鋼板に前記第一加熱室における加熱よりも高い温度の熱を加えるための空間を有する第二加熱室と、
前記第一加熱室と前記第二加熱室とを密閉して区画するとともに、第一加熱室から第二加熱室へ亜鉛メッキ鋼板を落下移動させる開閉手段と、
第一加熱室及び第二加熱室の外周に巻回され、前記第一加熱室及び前記第二加熱室において亜鉛メッキ鋼板に加熱を施すための加熱コイルとを備える
ことを特徴とする脱亜鉛装置。
A first heating chamber for applying heat to the galvanized steel sheet;
A second heating chamber located below the first heating chamber and having a space for applying heat at a temperature higher than the heating in the first heating chamber to the galvanized steel sheet heated in the first heating chamber When,
The first heating chamber and the second heating chamber are sealed and partitioned, and opening / closing means for dropping and moving the galvanized steel sheet from the first heating chamber to the second heating chamber;
A dezincing device comprising: a heating coil wound around the outer periphery of the first heating chamber and the second heating chamber and heating the galvanized steel sheet in the first heating chamber and the second heating chamber. .
前記脱亜鉛装置は、さらに、
前記第一加熱室の上方に位置し、亜鉛メッキ鋼板を投入するための投入口を有し、投入された亜鉛メッキ鋼板に前記第一加熱室における加熱よりも低い温度の熱を加えるための空間を有する予備加熱室を備え、
前記開閉手段は、前記予備加熱室と前記第一加熱室とを密閉して区画するとともに、予備加熱室から第一加熱室へ亜鉛メッキ鋼板を落下移動させる
ことを特徴とする請求項1記載の脱亜鉛装置。
The dezincing device further includes:
A space that is located above the first heating chamber, has an inlet for charging a galvanized steel sheet, and applies heat at a temperature lower than the heating in the first heating chamber to the input galvanized steel sheet A preheating chamber having
The said opening / closing means seals and partitions the said preheating chamber and said 1st heating chamber, and makes a galvanized steel plate fall and move from a preheating chamber to a 1st heating chamber. Dezincing equipment.
前記脱亜鉛装置は、さらに、
前記第二加熱室の下方に位置し、前記第二加熱室における加熱が施された亜鉛メッキ鋼板を滞留させる余熱室を備える
ことを特徴とする請求項1又は2記載の脱亜鉛装置。
The dezincing device further includes:
The dezincification apparatus according to claim 1 or 2, further comprising a preheating chamber that is located below the second heating chamber and retains the galvanized steel sheet that has been heated in the second heating chamber.
前記脱亜鉛装置は、さらに、
前記予備加熱室、前記第一加熱室、前記第二加熱室及び前記余熱室の少なくともいずれか1つに接続された排気パイプを備える
ことを特徴とする請求項3記載の脱亜鉛装置。
The dezincing device further includes:
The dezincification apparatus according to claim 3, further comprising an exhaust pipe connected to at least one of the preheating chamber, the first heating chamber, the second heating chamber, and the preheating chamber.
JP2009192989A 2009-08-24 2009-08-24 Dezincification apparatus Pending JP2011042851A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2009192989A JP2011042851A (en) 2009-08-24 2009-08-24 Dezincification apparatus
EP20090839046 EP2319946B1 (en) 2009-08-24 2009-12-11 Dezincing apparatus and dezincing method
PCT/JP2009/006785 WO2011024244A1 (en) 2009-08-24 2009-12-11 Dezincing apparatus and dezincing method
US12/833,412 US20110042371A1 (en) 2009-08-24 2010-07-09 Dezincing Apparatus and Dezincing Method

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04232216A (en) * 1990-12-28 1992-08-20 Shinko Electric Co Ltd Device for removing low melting point metal
JPH11223474A (en) * 1997-11-27 1999-08-17 Sms Schloeman Siemag Ag Steel scrap preheater for melting metallurgical furnace employing parallel flow of scrap and high temperature waste gas and process system thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04232216A (en) * 1990-12-28 1992-08-20 Shinko Electric Co Ltd Device for removing low melting point metal
JPH11223474A (en) * 1997-11-27 1999-08-17 Sms Schloeman Siemag Ag Steel scrap preheater for melting metallurgical furnace employing parallel flow of scrap and high temperature waste gas and process system thereof

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