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JP2008106344A - Method for manufacturing substrate for lead storage battery and manufacturing apparatus therefor - Google Patents

Method for manufacturing substrate for lead storage battery and manufacturing apparatus therefor Download PDF

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JP2008106344A
JP2008106344A JP2007018058A JP2007018058A JP2008106344A JP 2008106344 A JP2008106344 A JP 2008106344A JP 2007018058 A JP2007018058 A JP 2007018058A JP 2007018058 A JP2007018058 A JP 2007018058A JP 2008106344 A JP2008106344 A JP 2008106344A
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lead
substrate
melting
molten
furnace
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Akira Yamazaki
明 山崎
Shinya Suga
真也 菅
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Furukawa Battery Co Ltd
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Furukawa Battery Co Ltd
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • 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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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for manufacturing a substrate for a lead storage battery which inhibits the formation of dross in a melting/holding furnace for lead, and to provide a manufacturing apparatus therefor. <P>SOLUTION: The method for manufacturing the substrate 12 for the lead storage battery through the steps of casting molten lead or a lead alloy 5 which have been melted in the melting/holding furnace 1 into a grid substrate 12 by using a substrate-casting machine 2 includes the steps of: continuously melting a substrate-cut scrap 3 produced in the substrate-casting machine 2 while reducing the oxide of the surface; and returning the molten lead or the lead alloy to the melting/holding furnace 1. In an apparatus for manufacturing the substrate 12 for the lead storage battery, which has the melting/holding furnace 1 for lead or the lead alloy and a substrate-casting machine 2 as a main part, the apparatus for manufacturing the substrate 12 further has a continuous reductive melting furnace 4 for reducing and melting the oxide on the surface of a substrate-cut scrap 3 produced in the substrate-casting machine 2 and returning the molten lead or the lead alloy to the melting/holding furnace 1. The formation of the dross can be more adequately prevented by using a molten-lead recovery container or a lead scrap delivery machine. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、鉛または鉛合金の溶解保持炉におけるドロスの発生を低減した鉛蓄電池用基板の製造方法およびその製造装置に関する。   The present invention relates to a method for manufacturing a lead-acid battery substrate with reduced dross generation in a lead or lead alloy melting and holding furnace and a manufacturing apparatus therefor.

2枚の金型を用いた鉛蓄電池用格子基板の鋳造(ブックモールド鋳造)では、図3に示すように、鋳造したままの格子基板には溶湯を導入するための湯道部21と位置決めなどのための湯底部22が存在し、この湯道部21と湯底部22は鋳造後直ちに切除され、基板切除屑(以下、適宜、切除屑と記す。)として溶解保持炉に戻され再溶解して、再び格子基板に鋳造される。   In the casting of a lead-acid battery grid substrate using two molds (book mold casting), as shown in FIG. 3, the runner portion 21 for positioning the molten metal into the as-cast grid substrate and positioning, etc. The runner 21 and the bottom 22 are cut off immediately after casting and returned to the melting and holding furnace as substrate cutting scraps (hereinafter referred to as cutting scraps as appropriate) for remelting. Then, it is cast again on the lattice substrate.

この他、目切れ(湯不足に起因)、ボイド折れ、焼き折れなどの欠陥基板が発生した場合は、これも再溶解される。以下切除屑と欠陥基板を鉛屑と総称する。   In addition, if a defective substrate such as a break (due to lack of hot water), void breakage, or burnt breakage occurs, it is also re-dissolved. Hereinafter, the cut scrap and the defective substrate are collectively referred to as lead scrap.

このようにして鉛屑の再溶解を繰り返すうちに溶解保持炉の湯面にはドロスが多量に生成し浮遊するようになる。このドロスは溶解作業の邪魔になり、また製品への異物混入の原因になるため定期的に除去され、産業廃棄物として廃棄されている。
しかしながら、このドロスには80〜90mass%の高濃度の金属鉛が含まれているため、このドロスの廃棄は、製品のコストアップを招き、また資源の有効活用および環境保全の点でも問題があった。
このようなことから、ドロスの低減については、これまでに、種々提案(例えば、特許文献1)されているが、未だ、十分な効果が得られていない。
In this way, a large amount of dross is generated and floats on the molten metal surface of the melting and holding furnace while repeating the remelting of the lead scrap. The dross is a hindrance to the melting operation and also causes foreign matters to be mixed into the product. Therefore, the dross is periodically removed and discarded as industrial waste.
However, since this dross contains a high concentration of 80 to 90 mass% metallic lead, the disposal of this dross increases the cost of the product, and there are problems in terms of effective use of resources and environmental conservation. It was.
For these reasons, various proposals (for example, Patent Document 1) have been proposed to reduce dross, but a sufficient effect has not yet been obtained.

特開平9−73924号公報JP-A-9-73924

本発明者等は、かかる状況に鑑み、ドロスの発生原因の究明とその低減を目的に種々実験を行った。その結果、ドロスは鉛屑の表面の酸化物(膜)に起因して発生すること、鉛屑を還元性雰囲気で溶解してから溶解保持炉に戻すことでドロス量が低減することを知見し、さらに実験を重ねて本発明を完成させるに至った。
本発明は、鉛または鉛合金の溶解保持炉におけるドロスの発生を低減した鉛蓄電池用基板の製造方法およびその製造装置の提供を目的とする。
In view of this situation, the present inventors conducted various experiments for the purpose of investigating the cause of dross generation and reducing it. As a result, we found that dross is generated due to oxides (films) on the surface of lead scrap, and that the amount of dross is reduced by melting the lead scrap in a reducing atmosphere and then returning it to the melting and holding furnace. The present invention was completed through further experiments.
An object of this invention is to provide the manufacturing method of the board | substrate for lead acid batteries which reduced generation | occurrence | production of the dross in the melt | dissolution holding furnace of lead or a lead alloy, and its manufacturing apparatus.

請求項1記載発明は、溶解保持炉で溶解した鉛または鉛合金溶湯を基板鋳造機により格子基板に鋳造する鉛蓄電池用基板の製造方法において、前記基板鋳造機で発生する鉛屑を、その表面の酸化物を還元しながら連続的に溶解して溶解保持炉に戻すことを特徴とする鉛蓄電池用基板の製造方法である。   The invention according to claim 1 is a method for manufacturing a lead-acid battery substrate in which a molten lead or lead alloy melted in a melting and holding furnace is cast on a lattice substrate by a substrate casting machine. A method for producing a lead-acid battery substrate, wherein the oxide is continuously melted while being reduced and returned to the melting and holding furnace.

請求項2記載発明は、鉛または鉛合金溶解保持炉および基板鋳造機を主要部とする鉛蓄電池用基板の製造装置において、前記基板鋳造機で発生する鉛屑を、その表面の酸化物を還元しながら連続的に溶解して溶解保持炉に戻すための連続還元溶解炉が備えられていることを特徴とする鉛蓄電池用基板の製造装置である。   According to a second aspect of the present invention, there is provided a lead-acid battery substrate manufacturing apparatus mainly composed of a lead or lead alloy melting and holding furnace and a substrate casting machine, wherein lead scraps generated in the substrate casting machine are reduced with oxides on the surface thereof. An apparatus for producing a lead-acid battery substrate, comprising a continuous reduction melting furnace for continuously melting and returning to the melting holding furnace.

請求項3記載発明は、前記連続還元溶解炉は、内部が断面円形または断面矩形の筒状で、前記内部は高温の還元性ガス燃焼炎で充満されることを特徴とする請求項3または4に記載の鉛蓄電池用基板の製造装置である。   The invention according to claim 3 is characterized in that the continuous reduction melting furnace has a cylindrical shape with a circular cross section or a rectangular cross section, and the inside is filled with a high temperature reducing gas combustion flame. It is a manufacturing apparatus of the board | substrate for lead acid batteries as described in 1 ..

請求項4記載発明は、前記連続還元溶解炉には鉛屑投入口と溶湯出口が設けられており、前記鉛屑の溶融体が流動する床面が前記鉛屑投入口から溶湯出口に向けて下り勾配になっていることを特徴とする請求項2または3に記載の鉛蓄電池用基板の製造装置である。   According to a fourth aspect of the present invention, the continuous reduction melting furnace is provided with a lead scrap inlet and a molten metal outlet, and a floor surface on which the molten lead scrap flows from the lead scrap inlet to the molten metal outlet. The lead-acid battery substrate manufacturing apparatus according to claim 2 or 3, wherein the apparatus has a downward slope.

請求項5記載発明は、前記連続還元溶解炉の床面の上方に鉛屑を保持するためのスノコが設けられていることを特徴とする請求項2乃至4のいずれかに記載の鉛蓄電池用基板の製造装置である。   The invention according to claim 5 is a lead-acid battery according to any one of claims 2 to 4, wherein a slat for holding lead scraps is provided above the floor surface of the continuous reduction melting furnace. This is a substrate manufacturing apparatus.

請求項6記載発明は、前記連続還元溶解炉の溶湯出口から出湯する溶融鉛を回収するための両端開放の溶融鉛回収容器が、前記溶湯出口の下方、かつ前記溶解保持炉の湯面上に設けられていることを特徴とする請求項2乃至5のいずれかに記載の鉛蓄電池用基板の製造装置である。   According to a sixth aspect of the present invention, there is provided a molten lead recovery container opened at both ends for recovering molten lead discharged from the molten metal outlet of the continuous reduction melting furnace, below the molten metal outlet and on the molten metal surface of the melting holding furnace. It is provided, It is a manufacturing apparatus of the board | substrate for lead acid batteries in any one of the Claims 2 thru | or 5 characterized by the above-mentioned.

請求項7記載発明は、前記溶融鉛回収容器の溶解保持炉湯面からの突出距離Hが下記(1)および(2)式を満足することを特徴とする請求項6記載の鉛蓄電池用基板の製造装置である。
H≧20mm(1)
H≧h(h:連続還元溶解炉の溶湯出口下端と溶解保持炉内湯面間の距離)(2)
7. The lead storage battery substrate according to claim 6, wherein the protruding distance H of the molten lead recovery container from the melting and holding furnace surface satisfies the following expressions (1) and (2): It is a manufacturing apparatus.
H ≧ 20mm (1)
H ≧ h (h: distance between the lower end of the molten metal outlet of the continuous reduction melting furnace and the hot water surface in the melting and holding furnace) (2)

請求項8記載発明は、前記溶融鉛回収容器の内径Dと前記連続還元溶解炉の溶湯出口の内径dの比(D/d)が1.5〜3であることを特徴とする請求項6または7に記載の鉛蓄電池用基板の製造装置である。   The invention according to claim 8 is characterized in that the ratio (D / d) of the inner diameter D of the molten lead recovery vessel and the inner diameter d of the molten metal outlet of the continuous reduction melting furnace is 1.5-3. Or it is a manufacturing apparatus of the board | substrate for lead acid batteries of 7.

請求項9記載発明は、前記溶融鉛回収容器は横方向に開閉自在に分割されていることを特徴とする請求項6乃至8のいずれかに記載の鉛蓄電池用基板の製造装置である。   A ninth aspect of the present invention is the apparatus for manufacturing a lead-acid battery substrate according to any one of the sixth to eighth aspects, wherein the molten lead recovery container is divided so as to be openable and closable in the lateral direction.

請求項10記載発明は、前記連続還元溶解炉の上方に鉛屑送出機が設けられていることを特徴とする請求項2乃至9のいずれかに記載の鉛蓄電池用基板の製造装置である。   A tenth aspect of the present invention is the apparatus for manufacturing a lead-acid battery substrate according to any one of the second to ninth aspects, wherein a lead scrap feeder is provided above the continuous reduction melting furnace.

請求項1記載発明は、ブックモールドなどの鉛蓄電池用格子基板の鋳造機で発生する格子基板の鉛屑を、その表面の酸化物を還元し溶解して溶解保持炉に戻す鉛蓄電池用基板の製造方法であり、前記鉛屑は還元されているので、溶解保持炉でのドロスの発生量が低減する。従って製品のコストアップが抑えられ、また資源の有効活用および環境保全が計られる。   The invention according to claim 1 is a lead storage battery substrate in which lead scraps of a lattice substrate generated by a casting machine for a lead storage battery lattice substrate such as a book mold are returned to a melting and holding furnace by reducing oxides on the surface and dissolving them. In the manufacturing method, since the lead scrap is reduced, the amount of dross generated in the melting and holding furnace is reduced. Therefore, the cost increase of the product can be suppressed, and effective use of resources and environmental conservation can be achieved.

請求項2記載発明は、基板鋳造機で発生する鉛屑の表面の酸化物を還元し溶解して前記溶解保持炉に戻す連続還元溶解炉を備えた鉛蓄電池用基板の製造装置であり、前記鉛屑は、前記連続還元溶解炉により、その表面の酸化物が還元され、溶解されて溶解保持炉に戻されるので、溶解保持炉のドロス量が低減する。   The invention according to claim 2 is an apparatus for producing a lead-acid battery substrate comprising a continuous reduction melting furnace that reduces and melts oxides on the surface of lead scrap generated in a substrate casting machine and returns them to the melting and holding furnace. The lead scrap is reduced by the continuous reduction melting furnace, and the oxide on the surface thereof is melted and returned to the melting holding furnace, so that the dross amount of the melting holding furnace is reduced.

請求項3記載発明は、前記連続還元溶解炉の内部を断面円形または矩形の筒状とし、前記内部に高温の還元性ガス燃焼炎(以下、還元炎と略記する。)を充満させた鉛蓄電池用基板の製造装置なので、鉛屑は、その表面の酸化物が効率よく迅速に還元され溶解されて、溶解保持炉に戻される。   According to a third aspect of the present invention, there is provided a lead storage battery in which the inside of the continuous reduction melting furnace has a circular or rectangular cross section and is filled with a high temperature reducing gas combustion flame (hereinafter abbreviated as a reducing flame). Since this is an apparatus for manufacturing a substrate, the oxide on the surface of lead scrap is efficiently and rapidly reduced and melted, and returned to the melting and holding furnace.

請求項4記載発明は、前記連続還元溶解炉の鉛屑の溶融体が流動する床面を、切除屑投入口から溶湯出口に向けて下り勾配にしたものなので、鉛屑の溶融体は前記連続還元溶解炉内を溶湯出口に向けて迅速に移動し、作業性並びに生産性に優れる。   Since the floor surface in which the molten lead scrap of the continuous reduction melting furnace flows downward from the cutting scrap input port to the molten metal outlet, the lead scrap melt is the continuous scrap. It moves quickly in the reduction melting furnace toward the molten metal outlet and is excellent in workability and productivity.

請求項5記載発明は、連続還元溶解炉の床面上方にスノコを設けたもので、このスノコ上に鉛屑を保持すると、鉛屑の溶融体は液滴となってスノコ上から早々と落下して、鉛屑の未溶融部分から分離する。その結果、前記未溶融部分に還元炎が直射し、鉛屑の還元および溶解が効率よくなされる。   According to the fifth aspect of the present invention, the slats are provided above the floor surface of the continuous reduction melting furnace. When the lead scraps are held on the slats, the lead scrap melts as droplets and quickly drops from the slats. And separating from the unmelted portion of the lead scrap. As a result, a reducing flame directly shines on the unmelted portion, and lead scrap is efficiently reduced and dissolved.

請求項6記載発明は、前記請求項2乃至5のいずれかに記載の鉛蓄電池用基板の製造装置において、前記連続還元溶解炉の溶湯出口の下方、かつ前記溶解保持炉の鉛合金溶湯面上に両端開放の溶融鉛回収容器を設けたものであり、前記連続還元溶解炉の溶湯出口から落下する溶融鉛は前記溶融鉛回収容器内に落下し、かつ前記溶融鉛回収容器内は前記連続還元溶解炉から排出する非酸化性ガスが充満するため、前記溶湯出口から落下する溶融鉛は酸化およびドロス化が防止される。   A sixth aspect of the present invention is the apparatus for producing a lead-acid battery substrate according to any one of the second to fifth aspects, wherein the molten metal outlet of the continuous reduction melting furnace is below the lead alloy molten metal surface of the melting holding furnace. A molten lead recovery container open at both ends is provided, and the molten lead falling from the molten metal outlet of the continuous reduction melting furnace falls into the molten lead recovery container, and the molten lead recovery container is the continuous reduction Since the non-oxidizing gas discharged from the melting furnace is filled, the molten lead falling from the molten metal outlet is prevented from being oxidized and drossed.

この発明において、前記溶融鉛回収容器の溶解保持炉湯面からの突出距離Hが下記(1)および(2)式を満足することにより、前記溶融鉛回収容器内の雰囲気が、より非酸化性雰囲気になり、連続還元溶解炉から出湯する溶融鉛は酸化およびドロス化が安定して防止される。
H≧20mm(1)
H≧h(h:連続還元溶解炉の溶湯出口下端と溶解保持炉内湯面間の距離)(2)
In this invention, when the protrusion distance H of the molten lead recovery container from the melting and holding furnace surface satisfies the following expressions (1) and (2), the atmosphere in the molten lead recovery container is more non-oxidizing. The molten lead discharged from the continuous reduction melting furnace in an atmosphere is stably prevented from being oxidized and drossed.
H ≧ 20mm (1)
H ≧ h (h: distance between the lower end of the molten metal outlet of the continuous reduction melting furnace and the hot water surface in the melting and holding furnace) (2)

前記溶融鉛回収容器の内径Dと前記連続還元溶解炉の溶湯出口の内径dの比(D/d)を1.5〜3にすることにより、前記溶融鉛回収容器内の雰囲気がより非酸化性雰囲気になり、連続還元溶解炉から出湯する溶融鉛の酸化およびドロス化がより安定して防止される。   By setting the ratio (D / d) of the inner diameter D of the molten lead recovery container to the inner diameter d of the molten metal outlet of the continuous reduction melting furnace to be 1.5 to 3, the atmosphere in the molten lead recovery container is more non-oxidized. Thus, oxidation and dross formation of molten lead discharged from the continuous reduction melting furnace can be prevented more stably.

前記溶融鉛回収容器を横方向に開閉自在とすることにより、前記溶融鉛回収容器内のドロスを容易に掻き出すことができ、基板へのドロスの混入が防止できる。   By making the molten lead recovery container openable and closable in the lateral direction, dross in the molten lead recovery container can be scraped out easily, and mixing of dross into the substrate can be prevented.

請求項10記載発明は、連続還元溶解炉の上方に鉛屑送出機を設けた鉛蓄電池基板の製造装置であり、鉛屑は一旦前記鉛屑送出機に貯留されるため、欠陥基板などの鉛屑が連続して発生した場合でも、鉛屑が連続還元溶解炉から溢れ出て直接溶解保持炉に落下するようなことがなくなりドロスの発生がより確実に防止できる。またこの発明によれば欠陥基板を分別して後から連続還元溶解炉に投入するなどの作業が不要になるため、無人化運転が可能になる。   The invention according to claim 10 is a lead-acid battery substrate manufacturing apparatus provided with a lead scrap feeder above the continuous reduction melting furnace, and the lead scrap is temporarily stored in the lead scrap feeder, so that lead such as a defective substrate Even when scraps are continuously generated, lead scraps do not overflow from the continuous reduction melting furnace and directly fall into the melting and holding furnace, and dross generation can be prevented more reliably. In addition, according to the present invention, an operation such as sorting the defective substrates and subsequently putting them into the continuous reduction melting furnace becomes unnecessary, so that an unmanned operation is possible.

本発明は、鉛蓄電池用基板の鋳造後に発生する鉛屑を溶解保持炉に戻す際に、鉛屑表面の酸化物(膜)を還元しながら連続溶解して溶解保持炉に戻すようにした鉛蓄電池用基板の製造方法およびその製造装置であり、溶解保持炉でのドロスの発生量を低減し得るものである。   In the present invention, when lead waste generated after casting of a lead-acid battery substrate is returned to the melting and holding furnace, the oxide (film) on the surface of the lead scrap is continuously dissolved while being reduced and returned to the melting and holding furnace. A storage battery substrate manufacturing method and a manufacturing apparatus therefor, which can reduce the amount of dross generated in a melting and holding furnace.

本発明において、鉛屑を還元し溶解する方法には任意の方法が適用できるが、鉛屑に還元炎を放射する方法が簡便でありかつ生産性に優れ、推奨される。
前記還元炎には、例えば、メタンガス、エタンガス、プロパンガス、ブタンガス、都市ガスなどのガスの空燃比を制御してガス燃焼炎中のCO濃度を0.5〜5mass%に制御したものが適用できる。
In the present invention, any method can be applied as a method for reducing and dissolving lead scrap, but a method of radiating a reducing flame to lead scrap is simple and excellent in productivity and recommended.
As the reducing flame, for example, one in which the CO concentration in the gas combustion flame is controlled to 0.5 to 5 mass% by controlling the air-fuel ratio of gas such as methane gas, ethane gas, propane gas, butane gas, and city gas can be applied. .

本発明の鉛蓄電池用基板の製造装置は、図1に示すように、鉛または鉛合金溶解保持炉1、基板鋳造機2、基板鋳造機2で発生する鉛屑3の表面の酸化物を還元し溶解して溶解保持炉1に戻すための連続還元溶解炉4を主要部とする。
図1で5は鉛合金溶湯、6はコンベア、11は溶湯移送管、12は格子基板である。連続還元溶解炉4では鉛屑3内部に混在する酸化物も還元される。
The lead storage battery substrate manufacturing apparatus of the present invention reduces the oxides on the surface of the lead scrap 3 generated in the lead or lead alloy melting and holding furnace 1, the substrate casting machine 2, and the substrate casting machine 2, as shown in FIG. A continuous reduction melting furnace 4 for melting and returning to the melting holding furnace 1 is a main part.
In FIG. 1, 5 is a molten lead alloy, 6 is a conveyor, 11 is a molten metal transfer pipe, and 12 is a lattice substrate. In the continuous reduction melting furnace 4, oxides mixed inside the lead scrap 3 are also reduced.

連続還元溶解炉4は、図2に示すように、内部が断面円形の筒状で、筒状体の一端に鉛屑投入口4a、他端に溶湯出口4bが設けられ、内部に鉛屑3を保持するスノコ7が設けられ、鉛屑投入口4a部分にバーナー8が設けられ、バーナー8からは高温の還元炎9が放射される。連続還元溶解炉4の外周は断熱材10で形成されている。図2では溶湯移送管は図示を省略した。   As shown in FIG. 2, the continuous reduction melting furnace 4 has a cylindrical shape with a circular cross section, a lead scrap inlet 4 a at one end of the cylindrical body, a molten metal outlet 4 b at the other end, and lead scrap 3 inside. Is provided, and a burner 8 is provided at the lead scrap inlet 4a, and a high-temperature reducing flame 9 is emitted from the burner 8. The outer periphery of the continuous reduction melting furnace 4 is formed of a heat insulating material 10. In FIG. 2, the molten metal transfer pipe is not shown.

溶解保持炉1内の鉛合金溶湯5は、溶湯移送管11内を通って基板鋳造機2に導入されて格子基板12が連続的に金型鋳造される。格子基板12は直ちに不要部(切除屑3:湯道部21と湯底部22、図3参照)が切除されて次の極板工程に移送される。切除屑3はベルトコンベア6により連続還元溶解炉4の切除屑投入口4aに移送され、そこから連続還元溶解炉4内のスノコ7上に投下される。   The molten lead alloy 5 in the melting and holding furnace 1 is introduced into the substrate casting machine 2 through the molten metal transfer pipe 11, and the lattice substrate 12 is continuously die-cast. The grid substrate 12 is immediately cut away from unnecessary portions (cutting scrap 3: runner 21 and bottom 22, see FIG. 3) and transferred to the next electrode plate process. The cut waste 3 is transferred to the cut waste inlet 4a of the continuous reduction melting furnace 4 by the belt conveyor 6 and dropped from there onto the slats 7 in the continuous reduction melting furnace 4.

スノコ7上の切除屑3は高温の還元性ガス燃焼炎9により短時間のうちに表面の酸化物が還元されるとともに溶融し始める。溶融体は液滴3aとなってスノコ7上から床面4cに落下して切除屑3の未溶融部分から分離する。その結果、切除屑3の未溶融部分には還元炎9が直射し切除屑3が効率よく溶解する。液滴3aは集合して床面4c上を流動して溶湯出口4bに達し、そこから溶解保持炉1内に流入する。
目切れなどの欠陥基板が発生すれば切除屑3と同様に処理される。
The cutting waste 3 on the slat 7 begins to melt as the surface oxide is reduced in a short time by the high-temperature reducing gas combustion flame 9. The molten material becomes droplets 3 a and falls from the top of the slat 7 onto the floor surface 4 c and is separated from the unmelted portion of the cutting waste 3. As a result, the reducing flame 9 is directly applied to the unmelted portion of the cutting waste 3 and the cutting waste 3 is efficiently dissolved. The droplets 3 a gather and flow on the floor surface 4 c to reach the molten metal outlet 4 b and flow into the melting and holding furnace 1 from there.
If a defective substrate such as a break is generated, it is treated in the same manner as the cutting waste 3.

本発明において、連続還元溶解炉の構造は任意であり、例えば、内部を断面矩形の筒状として、その角部を下にして湯道(床面)としたものなども使用できる。
床面4cの傾斜角度αは20°以上にすることで溶融体が迅速に流動し望ましい。バーナー8の本数および設置箇所は、鉛屑の量や大きさに応じて適宜決定する。
In the present invention, the structure of the continuous reduction melting furnace is arbitrary. For example, the inside of the cylinder having a rectangular cross section and the corner of which is a downside (floor surface) can be used.
By setting the inclination angle α of the floor surface 4c to 20 ° or more, it is desirable that the melt quickly flows. The number and installation location of the burners 8 are appropriately determined according to the amount and size of lead scrap.

スノコには、比較的粗めの金網、多孔質材などが適用できる。スノコの傾斜角度βは切除屑などがスノコ上を円滑に滑り落ちる20°〜45°が適当である。45°を超えると切除屑などがスノコ上を転げ落ちて十分還元されずに溶解保持炉に落下する虞がある。   A relatively coarse wire mesh, a porous material, etc. can be applied to the slats. An appropriate inclination angle β of the slats is 20 ° to 45 ° where the cutting scraps smoothly slide on the slats. If the angle exceeds 45 °, cutting scraps or the like may fall on the slats and fall into the melting and holding furnace without being fully reduced.

図1、2に示した本発明の製造装置を用いて図3に示した格子基板を製造した。
溶解保持炉1により約2トンの鉛カルシウム合金を溶解し、溶湯温度を約500℃に保持した。湯面のドロスは鋳造開始前に完全に除去した。
The lattice substrate shown in FIG. 3 was manufactured using the manufacturing apparatus of the present invention shown in FIGS.
About 2 tons of lead calcium alloy was melted in the melting and holding furnace 1, and the molten metal temperature was kept at about 500 ° C. The dross on the molten metal surface was completely removed before casting was started.

連続還元溶解炉4内はバーナー8から放射されるブタンガスの還元炎9により約800℃に保持した。還元炎9は溶湯出口4bから溶解保持炉1の湯面に向けて排出させ溶解保持炉1の湯面上を覆うようにした。還元炎9のCOガス濃度はバーナー8の空燃比を調節して2〜3%に自動制御した。   The inside of the continuous reduction melting furnace 4 was maintained at about 800 ° C. by a reducing flame 9 of butane gas radiated from a burner 8. The reducing flame 9 was discharged from the molten metal outlet 4 b toward the molten metal surface of the melting and holding furnace 1 so as to cover the molten metal surface of the melting and holding furnace 1. The CO gas concentration in the reducing flame 9 was automatically controlled to 2 to 3% by adjusting the air-fuel ratio of the burner 8.

連続還元溶解炉4は、内部が断面円形(内径150mm)の筒状で、鉛屑投入口4aから溶湯出口4bまでの距離が1000mm、床面の傾斜角度αが30°、スノコの傾斜角度βが25°のものを用いた。   The continuous reduction melting furnace 4 has a cylindrical shape with a circular cross-section (inner diameter: 150 mm), a distance from the lead scrap inlet 4a to the molten metal outlet 4b is 1000 mm, a floor inclination angle α is 30 °, and a snowboard inclination angle β. With 25 °.

前記溶解保持炉1内の鉛合金溶湯5を、ポンプ(図示せず)により溶湯移送管11内を通して鋳造機2に送り、2枚の金型からなるブックモールド鋳造機により格子基板12を鋳造した。鋳造後、格子基板12は、直ちに不要部を切除して次の極板工程に移送した。切除した不要部(切除屑3)はベルトコンベア6により連続還元溶解炉4の切除屑投入口4aに移送し、そこから連続還元溶解炉4内のスノコ7上に投下した。なお、ここでは切除屑3のみを再溶解した。   The lead alloy molten metal 5 in the melting and holding furnace 1 is sent to the casting machine 2 through a molten metal transfer pipe 11 by a pump (not shown), and the lattice substrate 12 is cast by a book mold casting machine comprising two molds. . After casting, the grid substrate 12 was immediately cut off unnecessary parts and transferred to the next electrode plate process. The removed unnecessary part (cutting waste 3) was transferred to the cutting waste input port 4a of the continuous reduction melting furnace 4 by the belt conveyor 6 and dropped onto the slats 7 in the continuous reduction melting furnace 4 from there. Here, only excision waste 3 was redissolved.

切除屑3はスノコ6上でバーナー8から放射される高温の還元炎9により表面の酸化物が還元されるとともに表層が溶融し、溶融により自己潤滑性が増してスノコ6上を徐々に下方(溶湯出口方向)へと移動した。この間、切除屑3の溶融部分は液滴となってスノコ6の隙間から床面4cに落下し、床面4cの傾斜に沿って流動して溶湯出口4bから溶解保持炉1内に流入した。   The cutting waste 3 is reduced in the surface layer by the high-temperature reducing flame 9 radiated from the burner 8 on the slat 6 and the surface layer is melted. It moved to the molten metal outlet direction. During this time, the melted portion of the cutting waste 3 became droplets, dropped from the gap between the slats 6 to the floor surface 4c, flowed along the inclination of the floor surface 4c, and flowed into the melting and holding furnace 1 from the molten metal outlet 4b.

格子基板12は毎分17枚の速度で5時間に亘り鋳造した。溶解保持炉1内の溶湯5量は、鉛カルシウム合金インゴットを適宜投入してほぼ一定(約2トン)に保持した。切除屑3は1時間当たり100kg発生した。溶解保持炉1の湯面上に堆積したドロスは定期的に回収した。
鋳造終了後、回収した全ドロスを計量した。また前記全ドロス量を、溶解保持炉に戻した切除屑の量(500kg)で除してドロス発生率を求めた。
The lattice substrate 12 was cast at a rate of 17 sheets per minute for 5 hours. The amount of molten metal 5 in the melting and holding furnace 1 was kept substantially constant (about 2 tons) by appropriately introducing lead calcium alloy ingots. Excision waste 3 generated 100 kg per hour. Dross deposited on the surface of the melting and holding furnace 1 was periodically collected.
After the completion of casting, all recovered dross was weighed. The total dross amount was divided by the amount of cutting waste (500 kg) returned to the melting and holding furnace to determine the dross generation rate.

[比較例1]
切除屑3を、連続還元溶解炉4を通さずに、直接、溶解保持炉1に戻した他は、実施例1と同じ方法により格子基板12を鋳造し、また回収した全ドロスを計量してドロス発生率を求めた。
[Comparative Example 1]
The grid substrate 12 was cast by the same method as in Example 1 except that the cutting waste 3 was directly returned to the melting and holding furnace 1 without passing through the continuous reduction melting furnace 4, and all recovered dross was measured. The dross incidence was determined.

実施例1および比較例1の結果を表1に示す。   The results of Example 1 and Comparative Example 1 are shown in Table 1.

Figure 2008106344
Figure 2008106344

表1から明らかなように、本発明例(実施例1)ではドロス発生率が1%で、比較例1の4%に比べて大幅に低減した。これは、実施例1では、連続還元溶解炉を用いて、切除屑表面の酸化物を還元し溶解してから溶解保持炉に戻したことによる。   As is clear from Table 1, in the example of the present invention (Example 1), the dross generation rate was 1%, which was significantly reduced compared to 4% in Comparative Example 1. This is because, in Example 1, the continuous reduction melting furnace was used to reduce and melt the oxide on the surface of the cutting waste, and then returned to the melting holding furnace.

長時間操業の間には、連続還元溶解炉に投入される原料の増減によって、或いは溶解保持炉湯面上の気流の変化によって、連続還元溶解炉から排出される燃焼排ガス量が変動し、その結果、連続還元溶解炉出口から落下する溶融鉛が再酸化しドロス化することがある。請求項6に記載の発明は、連続還元溶解炉出口下方を安定して非酸化性雰囲気に保ち、連続還元溶解炉から落下する溶融鉛の再酸化およびドロス化を防止するための溶融鉛回収容器に関する。   During long-term operation, the amount of flue gas discharged from the continuous reduction melting furnace fluctuates due to the increase or decrease of the raw material charged into the continuous reduction melting furnace or the change of the air flow over the melting and holding furnace surface. As a result, molten lead falling from the outlet of the continuous reduction melting furnace may be reoxidized and drossed. The invention according to claim 6 is a molten lead recovery container for stably maintaining a non-oxidizing atmosphere below the outlet of the continuous reduction melting furnace and preventing reoxidation and drossing of molten lead falling from the continuous reduction melting furnace. About.

この発明の溶融鉛回収容器31は、例えば、図4(イ)に示すような両端開放の断面円形の容器であり、連続還元溶解炉4の下方に配置して用いられる。また、その下部は溶解保持炉1内の鉛合金溶湯5中に浸漬され、その中央部および上部は鉛合金溶湯面5a上に突出される。この溶融鉛回収容器31内には連続還元溶解炉4の溶湯出口4bから排出される非酸化性の燃焼排ガスが充満するため、連続還元溶解炉4の溶湯出口4bから落下する鉛合金溶湯5bは酸化およびドロス化が防止される。溶融鉛回収容器31の断面形状は円形に限らず、多角形状など任意である。図4(イ)において32は溶融鉛回収容器31を溶解保持炉1に取り付けるための部材である。   The molten lead recovery container 31 of the present invention is, for example, a container having a circular cross section open at both ends as shown in FIG. Moreover, the lower part is immersed in the molten lead alloy 5 in the melting and holding furnace 1, and the center part and the upper part protrude on the lead alloy molten metal surface 5a. Since the molten lead recovery container 31 is filled with non-oxidizing combustion exhaust gas discharged from the molten metal outlet 4b of the continuous reduction melting furnace 4, the lead alloy molten metal 5b falling from the molten metal outlet 4b of the continuous reduction melting furnace 4 is Oxidation and drossing are prevented. The cross-sectional shape of the molten lead recovery container 31 is not limited to a circular shape, and may be any polygonal shape. In FIG. 4A, 32 is a member for attaching the molten lead recovery container 31 to the melting and holding furnace 1.

この溶融鉛回収容器31は、図4(ロ)に示すように、その溶解保持炉1内の鉛合金溶湯面5aからの突出距離Hを20mm以上とし、かつ連続還元溶解炉4の溶湯出口4bの最下端部と溶解保持炉1の鉛合金溶湯面5aからの距離hと同等かそれ以上にすることにより溶融鉛回収容器31内に連続還元溶解炉4から排出される非酸化性の燃焼排ガスがより効率良く充満するようになる。   As shown in FIG. 4 (b), the molten lead recovery container 31 has a protruding distance H from the lead alloy molten metal surface 5 a in the melting and holding furnace 1 of 20 mm or more, and a molten metal outlet 4 b of the continuous reduction melting furnace 4. Non-oxidizing combustion exhaust gas discharged from the continuous reduction melting furnace 4 into the molten lead recovery vessel 31 by making it equal to or longer than the distance h from the lowermost end portion of the lead and the lead alloy molten metal surface 5a of the melting and holding furnace 1 Will fill more efficiently.

この発明において、溶融鉛回収容器31の内径Dと連続還元溶解炉の溶融鉛出口開口部の外径dの比(D/d)は、溶融鉛回収容器31内に非酸化性の燃焼排ガスを充満させるためには小さい方が良いが、あまり小さい(1に近づく)と溶融鉛回収容器31を所定位置に設けるのが困難になる。また比(D/d)が大きすぎると非酸化性の燃焼排ガスの拡散面積が増大して溶融鉛回収容器31内を非酸化性雰囲気に保持するのが困難になる。このようなことから比(D/d)は1.5〜3が望ましい。   In the present invention, the ratio (D / d) of the inner diameter D of the molten lead recovery container 31 and the outer diameter d of the molten lead outlet opening of the continuous reduction melting furnace is such that non-oxidizing combustion exhaust gas is introduced into the molten lead recovery container 31. In order to fill it up, it is better to be small, but if it is too small (close to 1), it is difficult to provide the molten lead recovery container 31 at a predetermined position. On the other hand, if the ratio (D / d) is too large, the diffusion area of the non-oxidizing combustion exhaust gas increases and it becomes difficult to maintain the inside of the molten lead recovery container 31 in a non-oxidizing atmosphere. Therefore, the ratio (D / d) is preferably 1.5 to 3.

この発明において、溶融鉛回収容器は、図5に示すように、溶融鉛回収容器33内のドロスを外部に容易に掻き出せるように横方向に開閉自在とすることが望ましい。溶融鉛回収容器33内にドロスが堆積すると、このドロスが落下する溶融鉛に混じって溶解保持炉1内の鉛合金溶湯5中に巻き込まれ鋳造基板の品質に悪影響を及ぼすので、溶融鉛回収容器33内は湯面を清浄にしておくことが望ましい。図5において33aは開閉部、33bは蝶番である。   In the present invention, as shown in FIG. 5, the molten lead recovery container is desirably openable and closable in the lateral direction so that the dross in the molten lead recovery container 33 can be easily scraped to the outside. When dross accumulates in the molten lead recovery vessel 33, the dross is mixed with the falling molten lead and is rolled into the molten lead alloy 5 in the melting and holding furnace 1 and adversely affects the quality of the cast substrate. In 33, it is desirable to keep the hot water surface clean. In FIG. 5, 33a is an opening / closing part, and 33b is a hinge.

図4(イ)、(ロ)に示した本発明の溶融鉛回収容器31を設けた製造装置を用いて連続溶解実験を5時間行ってドロスの発生量を実験により調べた。切除屑は実施例1と同様に1時間当たり100kg発生したので連続還元溶解炉で再溶解した切除屑は500kgである。溶解保持炉1の鉛合金溶湯面5a上のドロスは実験開始前に完全に除去しておいた。   Using the manufacturing apparatus provided with the molten lead recovery container 31 of the present invention shown in FIGS. 4 (a) and 4 (b), a continuous dissolution experiment was conducted for 5 hours to examine the amount of dross generated. As in Example 1, 100 kg of cutting waste was generated per hour, so that the cutting waste redissolved in the continuous reduction melting furnace was 500 kg. The dross on the molten lead surface 5a of the melting and holding furnace 1 was completely removed before the start of the experiment.

溶解保持炉1の内径は800mm、連続還元溶解炉2の出口4bは内径150mmの鉄製円筒(肉厚1mm)で構成し、その下端と溶解保持炉1の鉛合金溶湯面5aとの距離hは20mmに設定した。溶融鉛回収容器31は鉄製(肉厚1mm)で、その内径は100〜600mmの範囲で種々に変化させた。また、その溶解保持炉1の鉛合金溶湯面5aからの突出距離Hは10〜50mmの範囲で種々に変化させた。   The inner diameter of the melting and holding furnace 1 is 800 mm, and the outlet 4b of the continuous reduction melting furnace 2 is formed of an iron cylinder (thickness 1 mm) having an inner diameter of 150 mm, and the distance h between the lower end thereof and the lead alloy molten metal surface 5a of the melting and holding furnace 1 is Set to 20 mm. The molten lead recovery container 31 was made of iron (thickness 1 mm), and its inner diameter was variously changed in the range of 100 to 600 mm. Moreover, the protrusion distance H from the lead alloy molten metal surface 5a of the melting and holding furnace 1 was variously changed within a range of 10 to 50 mm.

(比較例2)
溶融鉛回収容器を設けなかった他は実施例1と同じ方法により切除屑を再溶解し、ドロスの発生量を調べた。
実施例2および比較例2の調査結果を表2に示す。
(Comparative Example 2)
Except that the molten lead recovery container was not provided, the excised waste was redissolved by the same method as in Example 1 and the amount of dross generated was examined.
The investigation results of Example 2 and Comparative Example 2 are shown in Table 2.

Figure 2008106344
Figure 2008106344

表2から明らかなように、溶融鉛回収容器を用いた実施例2(本発明例)では、ドロス量が3.00〜4.75kgと少なく、溶融鉛回収容器を用いない比較例1の5.13kgに較べてドロス量が7〜42%減少した。   As is apparent from Table 2, in Example 2 (example of the present invention) using the molten lead recovery container, the dross amount is as small as 3.00 to 4.75 kg, and 5 of Comparative Example 1 in which the molten lead recovery container is not used. The dross amount was reduced by 7 to 42% compared to .13 kg.

溶湯出口と鉛合金溶湯面との距離h(=20mm)に対し、溶融鉛回収容器の突出距離Hを10mm(No.5)と短い場合に比し20mm(No.4)と同等或いはそれ以上長くするとドロス量が急減することから、Hはhと同等又はそれ以上にすることが望ましい。また、突出距離Hが短いと連続還元溶解炉から落下する溶融鉛で溶融鉛回収容器内の湯面が揺動してドロスが回収容器から飛び出て鋳造基板に混入することがあることからも溶融鉛回収容器の突出距離Hは20mm以上にするのが望ましい。   Compared to the distance h (= 20 mm) between the molten metal outlet and the lead alloy molten metal surface, the protruding distance H of the molten lead recovery container is 10 mm (No. 5), which is equal to or more than 20 mm (No. 4). If the length is increased, the amount of dross decreases rapidly. Therefore, it is desirable that H is equal to or greater than h. Also, if the protruding distance H is short, the molten lead falling from the continuous reduction melting furnace may cause the molten metal surface in the molten lead recovery container to swing and the dross to jump out of the recovery container and enter the casting substrate. The protruding distance H of the lead recovery container is desirably 20 mm or more.

No.9はDが600mmと大きかったため燃焼排ガスの拡散面積が広くなり、溶融鉛回収容器内を十分な還元雰囲気に保持できずにドロス量がやや多めであったが、Dを450mmにしたNo.8(D/d=3.0)ではドロス量が著しく減少し、Dを180mmにしたNo.6(D/d=1.2)ではドロス量が最小となった。このように(D/d)の比は小さいほどドロス量は減少する。しかしながら、(D/d)が1に近づくと溶融鉛出口と溶融鉛回収容器の間隙が狭くなり溶融鉛回収容器を設けるのが困難になる。従って(D/d)の比は1.5〜3.0の範囲が望ましい。なお、実施例1では溶融鉛回収容器の突出距離Hを最大50mmとしたが、スペース的に問題なければさらに高くしても良い。   No. No. 9 had a large D of 600 mm, so the diffusion area of the combustion exhaust gas was widened, the molten lead recovery vessel could not be maintained in a sufficient reducing atmosphere, and the amount of dross was slightly larger. No. 8 (D / d = 3.0), the dross amount was remarkably reduced. At 6 (D / d = 1.2), the dross amount was minimized. Thus, the dross amount decreases as the ratio of (D / d) decreases. However, when (D / d) approaches 1, the gap between the molten lead outlet and the molten lead recovery container becomes narrow, making it difficult to provide a molten lead recovery container. Accordingly, the ratio of (D / d) is desirably in the range of 1.5 to 3.0. In Example 1, the protrusion distance H of the molten lead recovery container is set to 50 mm at the maximum, but may be further increased if there is no problem in terms of space.

図5に示した開閉自在の溶融鉛回収容器33を用いて24時間連続操業した。
この間、6時間ごとに溶融鉛回収容器33を開けてドロスを掻き出して回収容器33内の湯面5aを清浄化した。その結果、落下する溶融鉛に混じってドロスが溶解保持炉1内の鉛合金溶湯5中に巻き込まれるようなことがなく、品質良好な鋳造基板が安定して得られた。なお溶融鉛回収容器33の寸法および設置条件は実施例2のNo.6と同じにした。
Using the openable / closable molten lead recovery container 33 shown in FIG.
During this time, the molten lead recovery container 33 was opened every 6 hours and the dross was scraped to clean the hot water surface 5a in the recovery container 33. As a result, dross was not caught in the molten lead alloy 5 in the melting and holding furnace 1 mixed with the falling molten lead, and a cast substrate with good quality was stably obtained. The dimensions and installation conditions of the molten lead recovery container 33 are the same as those in Example 2. Same as 6.

長時間操業の中では、欠陥基板が連続して発生し、コンベヤにより搬送されてくる鉛屑が連続還元溶解炉に入り切らずに溢れ出て溶解保持炉に直接落下してしまうことがある。請求項10に記載の発明は欠陥基板が連続して発生した場合でも、鉛屑を連続還元溶解炉に安定して供給できる鉛屑送出機を設けた鉛蓄電池用基板の製造装置である。   During long-time operation, defective substrates are continuously generated, and lead scraps conveyed by the conveyor may overflow into the continuous reduction melting furnace and fall directly into the melting and holding furnace. A tenth aspect of the present invention is a lead-acid battery substrate manufacturing apparatus provided with a lead scrap feeder that can stably supply lead scrap to a continuous reduction melting furnace even when defective substrates are continuously generated.

前記鉛屑送出機41は、図6に示すように、ベルトコンベア6の鉛屑落下側の端部下方、かつ連続還元溶解炉4の鉛屑投入口4a上方に配置される。
鉛屑送出機41の構造は、図6、7に示すように、内面に攪拌羽42を設けたホッパー43と、ホッパー43の軸線上に配置された螺旋状のスクリュー47を備えたスクリューシャフト48を主要部とする。ホッパー43の鉛屑投入口43aの内径D(図7参照)はベルトコンベア6から落下する切除屑3などが漏れ出ないようにベルトコンベア6の幅よりも十分に大きくするのが良い。ホッパー43上端を漏斗状に拡げておくと切除屑3などの漏出がより確実に防げる。
As shown in FIG. 6, the lead scrap feeder 41 is disposed below the end of the belt conveyor 6 on the lead scrap dropping side and above the lead scrap inlet 4 a of the continuous reduction melting furnace 4.
As shown in FIGS. 6 and 7, the structure of the lead scrap delivery machine 41 is a screw shaft 48 including a hopper 43 provided with stirring blades 42 on the inner surface and a helical screw 47 arranged on the axis of the hopper 43. Is the main part. The inner diameter D 1 (see FIG. 7) of the lead scrap input port 43a of the hopper 43 is preferably made sufficiently larger than the width of the belt conveyor 6 so that the cutting waste 3 falling from the belt conveyor 6 does not leak. If the upper end of the hopper 43 is expanded in a funnel shape, leakage of the cutting waste 3 and the like can be prevented more reliably.

ホッパー43内面の攪拌羽42は、図8(イ)、(ロ)に示すように、水平方向に対し所定角度(θ)で傾斜して取り付けられている。攪拌羽42の先端面42aはホッパー43の軸線を中心とする円弧状に形成されている。
図8(イ)、(ロ)では、スクリューシャフト48は図示を省略してある。
ホッパー43は、図7に示すように、基台44に据付けられた電動機45により歯車46a、46bを介して矢印方向に低速で軸回転する。スクリューシャフト48は基台44に直接取り付けられ固定される。
As shown in FIGS. 8A and 8B, the stirring blade 42 on the inner surface of the hopper 43 is attached to be inclined at a predetermined angle (θ) with respect to the horizontal direction. The tip surface 42 a of the stirring blade 42 is formed in an arc shape centered on the axis of the hopper 43.
8A and 8B, the screw shaft 48 is not shown.
As shown in FIG. 7, the hopper 43 rotates at a low speed in the direction of the arrow through gears 46 a and 46 b by an electric motor 45 installed on the base 44. The screw shaft 48 is directly attached and fixed to the base 44.

コンベヤから落下する鉛屑は、ホッパー43の軸回転に伴って回転する攪拌羽42により攪拌されつつ、ホッパー43内を周回し、下方へと押出され排出口43cから排出される(図7参照)。前記鉛屑に掛かる下方への押出力は鉛屑とスクリュー47との間の摩擦により発生する。前記押出力は、撹拌羽42の傾斜角度θ、スクリュー47の角度αとピッチpなどを調整することにより制御される。   The lead scraps falling from the conveyor circulate in the hopper 43 while being stirred by the stirring blades 42 rotating with the shaft rotation of the hopper 43, and are pushed downward and discharged from the discharge port 43c (see FIG. 7). . The downward pushing force applied to the lead scrap is generated by friction between the lead scrap and the screw 47. The pushing force is controlled by adjusting the inclination angle θ of the stirring blade 42, the angle α of the screw 47, the pitch p, and the like.

この鉛屑送出機41によれば、鉛屑が多量に搬送されてきても、一旦ホッパー43内に貯留されてから排出されるので、鉛屑が連続還元溶解炉から溢れ出るようなことがない。また絡み合った鉛屑は攪拌羽42の回転により解きほぐされるので、鉛屑がスクリュー47と鉛屑排出口43cの間隙に詰まってしまうようなこともない。さらに鉛屑は撹拌羽42やスクリュー47により裁断されて細かくなるため連続還元溶解炉での溶解速度が向上する。   According to the lead scrap feeder 41, even if a large amount of lead scrap is conveyed, it is discharged after being stored in the hopper 43 once, so that the lead scrap does not overflow from the continuous reduction melting furnace. . Moreover, since the entangled lead scraps are unraveled by the rotation of the stirring blade 42, the lead scraps are not clogged in the gap between the screw 47 and the lead scrap discharge port 43c. Furthermore, since the lead scrap is cut by the stirring blade 42 and the screw 47 and becomes finer, the dissolution rate in the continuous reduction melting furnace is improved.

図7、図8(イ)、(ロ)に示した本発明の鉛屑送出機を用いて、その貯留機能を実験により調べた。
ホッパー43の鉛屑投入口43aの内径Dは400mm、貯留部43bの内径Dは500mm、鉛屑排出口43cの内径Dは150mm、ホッパー43の全高さHは500mmとした。ホッパー43内面の4枚の攪拌羽42の傾斜角度θは水平方向に対し45°とした。攪拌羽42先端面42aはR=200mmの円弧状とした。スクリュー47の外径Dは100mm、ピッチPは100mmとした。
The storage function of the lead scrap feeder according to the present invention shown in FIGS. 7, 8 (A) and 8 (B) was examined by experiment.
The inner diameter D 1 of the Namarikuzu inlet 43a of the hopper 43 is 400 mm, the inner diameter D 2 is 500mm in reservoir 43 b, the inner diameter D 3 of Namarikuzu outlet 43c is 150 mm, the total height H of the hopper 43 was 500mm. The inclination angle θ of the four stirring blades 42 on the inner surface of the hopper 43 was 45 ° with respect to the horizontal direction. The tip surface 42a of the stirring blade 42 was arc-shaped with R = 200 mm. Outer diameter D 4 of the screw 47 is 100 mm, the pitch P is set to 100 mm.

ベルトコンベヤ6(図6参照)により搬送されてくる切除屑と欠陥基板屑が混在した鉛屑を、毎分60回転するホッパー43の鉛屑投入口43aに毎分5kgずつ10分間に亘って合計50kg投入した。鉛屑は回転する攪拌羽42により解きほぐされながら下方に押出され、排出口43cから排出された。
鉛屑送出機41の排出口43cから排出される鉛屑を1分間単位で計量した。
その結果を図9に示した。
Lead scrap mixed with excavation scraps and defective substrate scraps conveyed by the belt conveyor 6 (see FIG. 6) is added to the lead scrap input port 43a of the hopper 43 that rotates 60 minutes per minute for 5 minutes per minute for 10 minutes. 50 kg was charged. The lead scrap was pushed downward while being unraveled by the rotating stirring blade 42 and discharged from the discharge port 43c.
Lead waste discharged from the discharge port 43c of the lead waste delivery machine 41 was measured in units of 1 minute.
The results are shown in FIG.

図9から明らかなように、鉛屑は、毎分5kgのペースで10分間投入され(線図a)、毎分4kgのペースで排出された(線図b)。この間ホッパー43内の鉛屑貯留量(線図c)は増加し続けた。鉛屑投入終了後はホッパー内の貯留量(線図c)は徐々に減少し、それに伴って排出量(線図b)も次第に減少し、20分後には貯留量および排出量ともゼロになった。図9で線図dはホッパー内に投入された鉛屑の累積量である。   As can be seen from FIG. 9, lead scrap was introduced for 10 minutes at a pace of 5 kg / min (diagram a) and discharged at a pace of 4 kg / min (diagram b). During this time, the amount of lead scrap stored in the hopper 43 (line c) continued to increase. The amount of storage in the hopper (line c) gradually decreases after the lead scrap is charged, and the amount of discharge (line b) gradually decreases along with it, and after 20 minutes, both the volume of storage and discharge become zero. It was. In FIG. 9, a line d is the cumulative amount of lead scrap introduced into the hopper.

図7、8(イ)、(ロ)に示した本発明の鉛屑送出機を用いて、一時に多量の鉛屑を投入したときの鉛屑の貯留機能を実験により調べた。
ホッパー内には、実操業を模して1分間当たり約1.7kgの切除屑を連続的に投入しつつ、投入開始2分後と5分後にそれぞれ欠陥基板屑10枚(約2kg)を追加投入し、10分後、17分後、18分後にそれぞれ欠陥基板屑20枚(約4kg)を追加投入した。鉛屑送出機41から排出される鉛屑量を1分間単位で計量した。
結果を図10に示した。
Using the lead scrap delivery device of the present invention shown in FIGS. 7, 8 (b) and (b), the storage function of lead scrap when a large amount of lead scrap was introduced at a time was examined by experiment.
Inside the hopper, approximately 1.7 kg of excavated scrap per minute was continuously fed to simulate actual operation, and 10 defective substrate scraps (approximately 2 kg) were added 2 and 5 minutes after the start of loading, respectively. Then, after 10 minutes, 17 minutes, and 18 minutes, 20 defective substrate scraps (about 4 kg) were additionally charged. The amount of lead waste discharged from the lead waste delivery machine 41 was measured in units of 1 minute.
The results are shown in FIG.

図10から明らかなように、排出量(線図b)は追加投入した直後に増加するが、その増加度合いは投入量(線図a)に較べて大幅に均されている。これによりホッパーの貯留機能が確認された。   As is clear from FIG. 10, the discharge amount (diagram b) increases immediately after the additional input, but the degree of increase is substantially equal to the input amount (diagram a). This confirmed the storage function of the hopper.

鉛蓄電池用基板の製造装置(図2参照)に、図7、8(イ)、(ロ)に示した本発明の鉛屑送出機を設けて(図6参照)、鉛蓄電池用基板を12時間に亘り連続的に製造した。ホッパー内には、実操業を模して1分間当たり約1.7kgの切除屑を連続的に投入し、この間に欠陥基板を複数枚ずつ10回追加投入した。   The lead storage battery substrate manufacturing apparatus (see FIG. 2) is provided with the lead scrap feeder according to the present invention shown in FIGS. 7, 8 (A) and (B) (see FIG. 6), and the lead storage battery substrate 12 Produced continuously over time. Into the hopper, approximately 1.7 kg of cut scraps per minute were continuously thrown into the hopper to simulate actual operation.

鉛屑はホッパー43内を攪拌羽42の回転に伴って下方へ移動し、排出口43cから連続還元溶解炉4内に送り込まれて溶解し、溶融鉛が液滴となって溶解保持炉1の鉛合金溶湯面5a上に落下した。
排出口43cからの鉛屑の排出量は、欠陥基板を追加投入した直後に増加するが、その増加度は小さく、鉛屑がホッパー43から溢れ出て溶解保持炉1に直接落下するなどのトラブルは発生しなかった。これにより鉛屑送出機は鉛屑を貯留する機能を有し、ドロス低減に有用なことが実証された。また連続還元溶解炉の周辺の無人化も実現可能なことが確認された。
Lead scrap moves downward in the hopper 43 as the stirring blades 42 rotate, and is sent into the continuous reduction melting furnace 4 from the discharge port 43c to be melted. The molten lead becomes droplets of the melting and holding furnace 1. It dropped on the lead alloy molten metal surface 5a.
The discharge amount of lead scrap from the discharge port 43c increases immediately after the additional defective substrate is added, but the increase is small, and trouble such as lead scrap overflowing from the hopper 43 and dropping directly into the melting and holding furnace 1 Did not occur. This proves that the lead scrap feeder has a function of storing lead scrap and is useful for dross reduction. It was also confirmed that unmanned operation around the continuous reduction melting furnace could be realized.

本発明では、図7、8(イ)、(ロ)に示した鉛屑送出機に限らず、鉛屑を貯留し、かつ排出する機能を有する任意の鉛屑送出機が適用できる。また鉛屑送出機のホッパーなどの設定条件(寸法や回転数)も上記実施例に限定されることなく、鉛屑の形状や量に応じて適宜選定することができる。さらに本発明では溶融鉛回収容器と鉛屑送出機を併用することによりドロスの発生をより良好に安定して防止することができる。   In the present invention, not only the lead scrap feeder shown in FIGS. 7, 8 (b) and (b), but any lead scrap feeder having a function of storing and discharging lead scrap can be applied. Further, the setting conditions (dimensions and rotation speed) of the hopper of the lead scrap feeder are not limited to the above-described embodiment, and can be appropriately selected according to the shape and amount of the lead scrap. Furthermore, in this invention, generation | occurrence | production of dross can be prevented more stably stably by using together a molten lead collection | recovery container and a lead waste sending machine.

本発明の鉛蓄電池用基板の製造装置の実施形態を示す平面説明図である。It is plane explanatory drawing which shows embodiment of the manufacturing apparatus of the board | substrate for lead acid batteries of this invention. 本発明の鉛蓄電池用基板の製造装置を構成する連続還元溶解炉の実施形態を示す側面説明図である。It is side explanatory drawing which shows embodiment of the continuous reduction melting furnace which comprises the manufacturing apparatus of the board | substrate for lead acid batteries of this invention. (イ)は鋳造したままの格子基板の実施形態を示す正面図、(ロ)は不要部を切除したあとの格子基板の実施形態を示す正面図である。(A) is a front view which shows embodiment of the lattice board | substrate as cast, (b) is a front view which shows embodiment of the lattice board | substrate after cutting an unnecessary part. (イ)は溶融鉛回収容器を設けた本発明の鉛蓄電池用基板の製造装置の実施形態を示す側面説明図、(ロ)は前記溶融鉛回収容器の側面説明図である。(A) is side explanatory drawing which shows embodiment of the manufacturing apparatus of the board | substrate for lead acid batteries of this invention which provided the molten lead collection | recovery container, (b) is side explanatory drawing of the said molten lead collection | recovery container. 前記溶融鉛回収容器の他の実施形態を示す平面説明図である。It is a plane explanatory view showing other embodiments of the molten lead recovery container. 鉛屑送出機を設けた本発明の鉛蓄電池用基板の製造装置の実施形態を示す側面説明図である。It is side explanatory drawing which shows embodiment of the manufacturing apparatus of the board | substrate for lead acid batteries of this invention which provided the lead waste sending machine. 前記鉛屑送出機の側面説明図である。It is side surface explanatory drawing of the said lead waste sending machine. 鉛屑送出機の撹拌羽部分の実施形態を示す、(イ)平面説明図、(ロ)側面説明図である。It is (I) plane explanatory drawing and (B) side explanatory drawing which show embodiment of the stirring blade part of a lead scrap sending machine. 鉛屑送出機の鉛屑の貯留量などの経時変化を示す説明図である。It is explanatory drawing which shows a time-dependent change, such as the storage amount of the lead scrap of a lead scrap sending machine. 鉛屑送出機の鉛屑の投入量と排出量の経時変化を示す説明図である。It is explanatory drawing which shows the time-dependent change of the input amount and discharge amount of the lead scrap of a lead scrap sending machine.

符号の説明Explanation of symbols

1 鉛または鉛合金溶解保持炉
2 基板鋳造機
3 切除屑
4 連続還元溶解炉
4a 鉛屑投入口
4b 溶湯出口
5 鉛合金溶湯
5a 鉛合金溶湯面
6 ベルトコンベア
7 スノコ
8 バーナー
9 還元性ガス燃焼炎(還元炎)
10 断熱材
11 溶湯移送管
12 格子基板(鉛蓄電池用基板)
21 湯道部(不要部)
22 湯底部(不要部)
31 溶融鉛回収容器
32 溶融鉛回収容器を溶解保持炉に取り付けるための部材
33 横方向に開閉自在な溶融鉛回収容器
33a 溶融鉛回収容器の開閉部
33b 溶融鉛回収容器の蝶番
41 鉛屑送出機
42 攪拌羽
42a 攪拌羽の先端面
43 ホッパー
43a ホッパーの鉛屑投入口
43b ホッパーの貯留部
43c ホッパーの鉛屑排出口
44 基台
45 電動機(駆動源)
46a、46b 歯車
47 スクリュー
48 スクリューシャフト
1 Lead or lead alloy melting and holding furnace 2 Substrate casting machine 3 Cutting scrap 4 Continuous reduction melting furnace 4a Lead scrap charging port 4b Molten metal outlet 5 Lead alloy molten metal 5a Lead alloy molten metal surface 6 Belt conveyor 7 Snowboard 8 Burner 9 Reducing gas combustion flame (Reducing flame)
10 Heat Insulation Material 11 Molten Metal Transfer Pipe 12 Lattice Substrate (Lead Storage Battery Substrate)
21 runway (unnecessary part)
22 Hot water bottom (unnecessary part)
31 Molten lead recovery container 32 Member 33 for attaching the molten lead recovery container to the melting and holding furnace Molten lead recovery container 33a openable and closable in the lateral direction Opening and closing part 33b of the molten lead recovery container Hinge 41 of the molten lead recovery container Lead scrap delivery machine 42 Stirring vane 42a Stirring vane front end surface 43 Hopper 43a Hopper lead waste inlet 43b Hopper reservoir 43c Hopper lead waste outlet 44 Base 45 Electric motor (drive source)
46a, 46b Gear 47 Screw 48 Screw shaft

Claims (10)

溶解保持炉で溶解した鉛または鉛合金溶湯を基板鋳造機により格子基板に鋳造する鉛蓄電池用基板の製造方法において、前記基板鋳造機で発生する鉛屑を、その表面の酸化物を還元しながら連続的に溶解して溶解保持炉に戻すことを特徴とする鉛蓄電池用基板の製造方法。   In a method for manufacturing a lead-acid battery substrate in which molten lead or lead alloy melted in a melting holding furnace is cast on a lattice substrate by a substrate casting machine, lead oxide generated in the substrate casting machine is reduced while reducing oxides on the surface thereof. A method for producing a substrate for a lead-acid battery, characterized by being continuously melted and returned to a melting and holding furnace. 鉛または鉛合金溶解保持炉および基板鋳造機を主要部とする鉛蓄電池用基板の製造装置において、前記基板鋳造機で発生する鉛屑を、その表面の酸化物を還元しながら連続的に溶解して溶解保持炉に戻すための連続還元溶解炉が備えられていることを特徴とする鉛蓄電池用基板の製造装置。   In a lead or battery substrate manufacturing apparatus mainly composed of a lead or lead alloy melting and holding furnace and a substrate casting machine, lead scrap generated in the substrate casting machine is continuously dissolved while reducing oxides on the surface. An apparatus for producing a lead-acid battery substrate, comprising a continuous reduction melting furnace for returning to the melting and holding furnace. 前記連続還元溶解炉は、内部が断面円形または断面矩形の筒状で、前記内部は高温の還元性ガス燃焼炎で充満されることを特徴とする請求項2に記載の鉛蓄電池用基板の製造装置。   The lead-acid battery substrate according to claim 2, wherein the continuous reduction melting furnace has a cylindrical shape with a circular cross-section or a rectangular cross-section, and the inside is filled with a high-temperature reducing gas combustion flame. apparatus. 前記連続還元溶解炉には鉛屑投入口と溶湯出口が設けられており、前記鉛屑の溶融体が流動する床面が前記鉛屑投入口から溶湯出口に向けて下り勾配になっていることを特徴とする請求項2または3に記載の鉛蓄電池用基板の製造装置。   The continuous reduction melting furnace is provided with a lead scrap inlet and a molten metal outlet, and the floor on which the molten lead scrap flows is downwardly inclined from the lead scrap inlet to the molten metal outlet. The manufacturing apparatus of the board | substrate for lead acid batteries of Claim 2 or 3 characterized by these. 前記連続還元溶解炉の床面の上方に鉛屑を保持するためのスノコが設けられていることを特徴とする請求項2乃至4のいずれかに記載の鉛蓄電池用基板の製造装置。   The apparatus for producing a substrate for a lead storage battery according to any one of claims 2 to 4, wherein a slat for holding lead scraps is provided above the floor surface of the continuous reduction melting furnace. 前記連続還元溶解炉の溶湯出口から出湯する溶融鉛を回収するための両端開放の溶融鉛回収容器が、前記溶湯出口の下方、かつ前記溶解保持炉の湯面上に設けられていることを特徴とする請求項2乃至5のいずれかに記載の鉛蓄電池用基板の製造装置。   A molten lead recovery container open at both ends for recovering molten lead discharged from the molten metal outlet of the continuous reduction melting furnace is provided below the molten metal outlet and on the molten metal surface of the melting holding furnace. The manufacturing apparatus of the board | substrate for lead acid batteries in any one of Claim 2 thru | or 5. 前記溶融鉛回収容器の溶解保持炉湯面からの突出距離Hが下記(1)および(2)式を満足することを特徴とする請求項6記載の鉛蓄電池用基板の製造装置。
H≧20mm(1)
H≧h(h:連続還元溶解炉の溶湯出口下端と溶解保持炉内湯面間の距離)(2)
The apparatus for producing a substrate for a lead storage battery according to claim 6, wherein a protruding distance H of the molten lead recovery container from the melting and holding furnace surface satisfies the following expressions (1) and (2).
H ≧ 20mm (1)
H ≧ h (h: distance between the lower end of the molten metal outlet of the continuous reduction melting furnace and the hot water surface in the melting and holding furnace) (2)
前記溶融鉛回収容器の内径Dと前記連続還元溶解炉の溶湯出口の内径dの比(D/d)が1.5〜3であることを特徴とする請求項6または7に記載の鉛蓄電池用基板の製造装置。   The lead acid battery according to claim 6 or 7, wherein a ratio (D / d) of an inner diameter D of the molten lead recovery container and an inner diameter d of a molten metal outlet of the continuous reduction melting furnace is 1.5 to 3. Board manufacturing equipment. 前記溶融鉛回収容器は横方向に開閉自在に分割されていることを特徴とする請求項6乃至8のいずれかに記載の鉛蓄電池用基板の製造装置。   The lead-acid battery substrate manufacturing apparatus according to any one of claims 6 to 8, wherein the molten lead recovery container is divided to be openable and closable in a lateral direction. 前記連続還元溶解炉の上方に鉛屑送出機が設けられていることを特徴とする請求項2乃至9のいずれかに記載の鉛蓄電池用基板の製造装置。   The lead-acid battery substrate manufacturing apparatus according to any one of claims 2 to 9, wherein a lead scrap feeder is provided above the continuous reduction melting furnace.
JP2007018058A 2006-09-25 2007-01-29 Method for manufacturing substrate for lead storage battery and manufacturing apparatus therefor Pending JP2008106344A (en)

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JPS558451A (en) * 1978-07-03 1980-01-22 Furukawa Electric Co Ltd:The Melting apparatus of lead and lead alloy
JPH01234530A (en) * 1988-03-14 1989-09-19 Fujikura Ltd Automatically controlled melting furnace
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CN109261947A (en) * 2018-11-27 2019-01-25 湖南水口山有色金属集团有限公司 A kind of lead liquid transportation system

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