JP2009007622A - Method for melting lead scrap, and method for manufacturing substrate for lead battery and manufacturing method thereof - Google Patents

Method for melting lead scrap, and method for manufacturing substrate for lead battery and manufacturing method thereof Download PDF

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JP2009007622A
JP2009007622A JP2007169645A JP2007169645A JP2009007622A JP 2009007622 A JP2009007622 A JP 2009007622A JP 2007169645 A JP2007169645 A JP 2007169645A JP 2007169645 A JP2007169645 A JP 2007169645A JP 2009007622 A JP2009007622 A JP 2009007622A
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lead
scrap
melting
holding furnace
receiving container
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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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

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  • Manufacture And Refinement Of Metals (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Cell Electrode Carriers And Collectors (AREA)
  • Secondary Cells (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for melting lead scrap while suppressing the formation of dross and also to provide a method for manufacturing a substrate for a lead battery using the melting method. <P>SOLUTION: In the method for melting lead scrap, a lead scrap receiving container 2 having a recessed longitudinal section and an opening 2a in the bottom is disposed on a lead or lead alloy melting and holding furnace 1, and lead scrap 4 is fed into the container 2 and heated and melted by a reducing flame, and the resulting melt is allowed to flow gently into molten lead 1d in the melting and holding furnace 1. In the method for manufacturing a substrate for a lead battery where the molten lead or lead alloy 1d melted in the melting and holding furnace 1 is cast into a grating substrate using a substrate casting machine 7, the lead scrap 4 generated in the substrate casting machine 7 is fed into the lead scrap receiving container 2 which has a recessed longitudinal section and an opening 2a in the bottom and disposed on the melting and holding furnace 1, where the lead scrap 4 is heated and melted by a reducing flame and the resulting melt is allowed to flow gently into the molten lead or lead alloy 1d in the melting and holding furnace 1 through the opening 2a of the lead scrap receiving container 2. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、ドロスの発生を低減した鉛屑の溶解方法、前記溶解方法を用い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 melting lead debris with reduced dross generation, a method for manufacturing a lead-acid battery substrate using the melting method, and a manufacturing apparatus therefor.

2枚の金型(ブックモールド)を用いて鋳造した鉛蓄電池用格子基板8には、図6(イ)に示すように、鉛溶湯を導入するための湯道部8aと位置決めなどのための湯底部8bが存在し、これらは鋳造後直ちに切除され、この切除屑(鉛屑)は図7、8に示すようにコンベア3により移送されて溶解保持炉1の鉛屑投入室1aに投入(落下)されて再溶解され、溶湯移送管6を経て鋳造機7に送られて再び格子基板に鋳造される。再溶解される鉛屑4には、前記切除屑の他、目切れ(湯不足)、ボイド折れ、焼き折れなどの欠陥基板も含まれる。図7、8で、1dは鉛溶湯、1cは鉛屑投入室1aとインゴット投入室1bとを上部で仕切る仕切板である。   As shown in FIG. 6 (a), the lead storage battery lattice substrate 8 cast using two molds (book molds) has a runner portion 8a for introducing molten lead and positioning. As shown in FIGS. 7 and 8, the cut scraps (lead scrap) are transferred by the conveyor 3 and put into the lead scrap input chamber 1a of the melting and holding furnace 1 (see FIG. 7 and FIG. 8). It is dropped) and remelted, sent to the casting machine 7 through the molten metal transfer pipe 6, and cast again on the lattice substrate. The lead scrap 4 to be remelted includes defective substrates such as cuts (insufficient hot water), void breakage, and burnt breakage in addition to the excision waste. 7 and 8, 1d is a molten lead, and 1c is a partition plate that partitions the lead scrap charging chamber 1a and the ingot charging chamber 1b at the top.

このようにして鉛屑4の再溶解を繰り返すうちに溶解保持炉1の湯面にはドロスが多量に浮遊してくる。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も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、このドロスを廃棄することは、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)されてきたが、未だ、十分な効果が得られていない。
In this way, a lot of dross floats on the surface of the melting and holding furnace 1 while repeating the remelting of the lead scrap 4. Since this dross interferes with the melting operation and also causes foreign matter to enter the product, it is periodically removed and discarded as industrial waste.
However, since this dross contains high-concentration lead of 80 to 90 mass%, discarding this dross leads to an increase in the cost of the product, and there are problems in terms of effective use of resources and environmental conservation. was there.
For this reason, various proposals (for example, Patent Document 1) have been proposed for reducing 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て種々実験を行った。その結果ドロスの主な発生原因が、鉛屑表面に存在する酸化膜、鉛屑が落下する際に巻き込まれる大気、鉛屑が落下する際の湯面の波立ち(乱れ)などであることを突き止め、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、ドロスの発生を低減し得る鉛屑の溶解方法、前記溶解方法を用い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。
The present inventors conducted various experiments in view of this situation. As a result, we found out that the main causes of dross are the oxide film present on the surface of the lead scrap, the atmosphere that is involved when the lead scrap falls, and the undulation (turbulence) of the molten metal surface when the lead scrap falls. The present invention was completed through further experiments.
An object of the present invention is to provide a lead scrap melting method capable of reducing the generation of dross, a method for manufacturing a lead-acid battery substrate using the melting method, and a manufacturing apparatus therefor.

請求項1記載発明は、鉛または鉛合金溶解保持炉上に縦断面が凹状で底部に開口部を有する鉛屑受け容器を配し、前記鉛屑受け容器内に鉛屑を供給し、前記鉛屑を還元炎で加熱溶融し、この鉛屑の溶融体を前記鉛屑受け容器の開口部から溶解保持炉内の鉛または鉛合金溶湯中に静かに流入させることを特徴とする鉛屑の溶解方法である。   According to a first aspect of the present invention, a lead scrap receiving container having a concave longitudinal section and having an opening at the bottom is disposed on a lead or lead alloy melting and holding furnace, the lead scrap is supplied into the lead scrap receiving container, and the lead Dissolution of lead scraps, characterized in that the scraps are heated and melted with a reducing flame, and the lead scrap melt is gently poured into the lead or lead alloy melt in the melting and holding furnace through the opening of the lead scrap receiving container. Is the method.

請求項2記載発明は、前記鉛屑受け容器の底部を溶解保持炉内の鉛または鉛合金溶湯中に浸入させることを特徴とする請求項1に記載の鉛屑の溶解方法である。   According to a second aspect of the present invention, there is provided the lead scrap melting method according to the first aspect, wherein the bottom portion of the lead scrap receiving container is allowed to enter a lead or lead alloy molten metal in a melting and holding furnace.

請求項3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用いて基板鋳造機により格子基板を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、前記溶解保持炉上に配した縦断面が凹状で底部に開口部を有する鉛屑受け容器内に供給し、前記鉛屑を還元炎で加熱溶融し、この鉛屑の溶融体を前記鉛屑受け容器の開口部から溶解保持炉内の鉛または鉛合金溶湯中に静かに流入させることを特徴とする鉛蓄電池用基板の製造方法である。   A third aspect of the present invention is a method for manufacturing a substrate for a lead storage battery in which a lattice substrate is cast by a substrate casting machine using lead or a lead alloy molten metal melted in a melting holding furnace, wherein lead scrap generated in the substrate casting machine is A vertical cross section disposed on the melting and holding furnace is concave and is supplied into a lead scrap receiving container having an opening at the bottom, the lead scrap is heated and melted with a reducing flame, and the molten lead scrap is received by the lead scrap receiver. A lead storage battery substrate manufacturing method characterized by gently flowing into lead or lead alloy molten metal in a melting and holding furnace from an opening of a container.

請求項4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装置において、前記溶解保持炉上に、縦断面が凹状で底部に開口部を有する鉛屑受け容器および前記鉛屑受け容器内の鉛屑を還元炎で加熱溶融するためのバーナー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 fourth aspect of the present invention, there is provided an apparatus for producing 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. And a burner for heating and melting the lead scrap in the lead scrap receiving container with a reducing flame.

請求項5記載発明は、前記鉛屑受け容器が鉄系またはステンレス系の金属材料で構成されていることを特徴とする請求項4に記載の鉛蓄電池用基板の製造装置である。   A fifth aspect of the present invention is the apparatus for manufacturing a lead-acid battery substrate according to the fourth aspect, wherein the lead scrap receiving container is made of an iron-based or stainless-based metal material.

請求項6記載発明は、バーナーが2基以上備えられていることを特徴とする請求項4または5に記載の鉛蓄電池用基板の製造装置である。   The invention according to claim 6 is the apparatus for producing a substrate for a lead storage battery according to claim 4 or 5, wherein two or more burners are provided.

本発明の鉛屑の溶解方法は、鉛または鉛合金溶解保持炉上に縦断面が凹状で底部に開口部を有する鉛屑受け容器を配し、前記容器内に鉛屑を供給し、前記鉛屑を還元炎で加熱溶融するので、鉛屑表面の酸化膜が除去される。またこの鉛屑の溶融物を溶解保持炉内の鉛溶湯中に静かに流入させるので、溶解保持炉内の鉛溶湯に大気が巻き込まれたり、鉛溶湯面が波立ったりしない。従って溶解保持炉でのドロスの発生量が低減する。さらに鉛屑受け容器が凹状のためコンベアから落下する鉛屑は鉛屑受け容器内に効率良くかつ良好に保持される。   In the lead scrap melting method of the present invention, a lead scrap receiving container having a concave longitudinal section and having an opening at the bottom is disposed on a lead or lead alloy melting and holding furnace, the lead scrap is supplied into the container, and the lead Since the scrap is heated and melted with a reducing flame, the oxide film on the surface of the lead scrap is removed. Further, since the molten lead scrap is gently allowed to flow into the molten lead in the melting and holding furnace, the atmosphere does not get involved in the molten lead in the melting and holding furnace, and the molten lead surface does not wave. Therefore, the amount of dross generated in the melting and holding furnace is reduced. Furthermore, since the lead scrap receiving container is concave, the lead scrap falling from the conveyor is efficiently and satisfactorily held in the lead scrap receiving container.

本発明の鉛屑の溶解方法では、前記鉛屑受け容器の底部を溶解保持炉内の鉛溶湯に浸入させることにより、前記鉛屑受け容器内の鉛屑は前記鉛溶湯と接触して迅速に溶解する。また前記鉛屑受け容器は溶解保持炉内の鉛溶湯の熱を受け易くなり熱効率が向上する。また溶融した鉛屑は開口部を通って溶解保持炉内の鉛溶湯に静かに移動し大気の巻き込みや鉛溶湯の波立ちなどがより良好に防止される。
さらに鉛屑が鉛屑受け溶器内の鉛溶湯に直接落下したとしても、それによる大気の巻込みおよび鉛溶湯の波立ちは鉛屑受け容器内に制限される(図3(イ)参照)。そのためドロスの発生は極めて良好に防止される。
In the lead scrap melting method of the present invention, the bottom of the lead scrap receiving container is infiltrated into the molten lead in the melting and holding furnace so that the lead scrap in the lead scrap receiving container comes into contact with the molten lead quickly. Dissolve. In addition, the lead scrap receiving container can easily receive the heat of the molten lead in the melting and holding furnace, and the thermal efficiency is improved. Also, the molten lead scraps gently move to the molten lead in the melting and holding furnace through the opening, and the air entrainment and the spilling of the molten lead are better prevented.
Furthermore, even if lead scrap falls directly on the molten lead in the lead scrap receiving fuser, the entrainment of the air and the undulation of the lead molten metal are restricted in the lead scrap receiving container (see FIG. 3 (A)). Therefore, dross generation is prevented very well.

本発明の鉛蓄電池用基板の製造方法では、鉛屑を、溶解保持炉上に配した縦断面が凹状で底部に開口部を有する鉛屑受け容器内に供給し還元炎で加熱溶融するので鉛屑表面の酸化膜が還元される。また鉛屑の溶融体は溶解保持炉内の鉛または鉛合金溶湯(以下鉛溶湯と略記)中に静かに流入させるので溶解保持炉内の鉛溶湯に大気が巻き込まれたり、鉛溶湯面が波立ったりしない。従って溶解保持炉でのドロスの発生量が低減し、製品のコストダウン、資源の有効活用、環境保全が計れる。   In the method for manufacturing a substrate for a lead storage battery of the present invention, lead scrap is supplied to a lead scrap receiving container having a concave longitudinal section arranged on a melting and holding furnace and having an opening at the bottom, and is heated and melted with a reducing flame. The oxide film on the scrap surface is reduced. Also, the molten lead scrap gently flows into the lead or lead alloy molten metal (hereinafter abbreviated as lead molten metal) in the melting and holding furnace. Do not stand. Therefore, the amount of dross generated in the melting and holding furnace can be reduced, and the cost of the product can be reduced, the resources can be effectively used, and the environment can be protected.

本発明の鉛蓄電池用基板の製造装置は、従来の製造装置の溶解保持炉上に、縦断面が凹状で底部に開口部を有する鉛屑受け容器を配し、そこにバーナーを備えただけのもので、スペース的にも、コスト的にも優れる。   The lead storage battery substrate manufacturing apparatus according to the present invention has a lead scrap receiving container with a concave longitudinal section and an opening at the bottom on a melting and holding furnace of a conventional manufacturing apparatus, and is simply provided with a burner. It is excellent in terms of space and cost.

前記鉛屑受け容器は、鉄系またはステンレス系の金属材料で構成することにより、溶解保持炉の構造に合った形状に容易に形成でき、また容器の耐久性が向上し、さらに鉄系材料は廉価である。   The lead scrap receiving container can be easily formed into a shape suitable for the structure of the melting and holding furnace by being composed of an iron-based or stainless-based metal material, and the durability of the container is improved. Inexpensive.

前記鉛屑受け容器にバーナーを2本以上備えることにより、前記鉛屑受け容器内に還元炎がより良好に充満し、鉛屑表面の酸化膜の還元が良好になされ、しかも溶解速度が向上する。   By providing two or more burners in the lead scrap receiving container, the lead scrap receiving container is more satisfactorily filled with the reducing flame, the oxide film on the lead scrap surface is reduced, and the dissolution rate is improved. .

本発明の鉛屑の溶解方法の実施形態を、図1を参照して説明する。
加温され鉛または鉛合金を溶解保持する鉛または鉛合金溶解保持炉1上に縦断面が凹状で底部に開口部を有する鉛屑受け容器2を配し、コンベア3で移送されてくる鉛屑4を鉛屑受け容器2内に供給し、鉛屑4をバーナー5から噴射される還元炎5aで加熱溶融し、この鉛屑溶融体を溶解保持炉内の鉛溶湯1d中に静かに流入させる。
An embodiment of the lead scrap melting method of the present invention will be described with reference to FIG.
Lead scrap receiving container 2 having a concave longitudinal section and having an opening at the bottom is disposed on lead or lead alloy melting and holding furnace 1 which is heated and melts and holds lead or lead alloy, and lead scrap transferred by conveyor 3 4 is supplied into the lead scrap receiving container 2, the lead scrap 4 is heated and melted by the reducing flame 5 a injected from the burner 5, and the lead scrap melt is gently poured into the molten lead 1 d in the melting and holding furnace. .

鉛屑受け容器2内に供給された鉛屑4はバーナー5から噴射される高温の還元性ガス燃焼炎(還元炎)5a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。溶融した鉛屑4は開口部2aから溶解保持炉1の鉛屑投入室1a内に流れ落ちる(流入する)。   The lead scrap 4 supplied into the lead scrap receiving container 2 starts to melt while the surface oxide is reduced in a short time by the high-temperature reducing gas combustion flame (reducing flame) 5a injected from the burner 5. . The molten lead scrap 4 flows down (inflows) from the opening 2 a into the lead scrap charging chamber 1 a of the melting and holding furnace 1.

図1において、鉛屑受け容器2の開口部2aの下端と鉛屑投入室1a内の鉛溶湯1dの湯面との距離dは50mm以下が望ましい。dが50mmを超えると鉛屑溶湯の流落量によっては大気の巻き込み、湯面の波立ちが起きる場合がある。ここでは鉛屑受け容器2は、溶解保持炉1内の鉛溶湯1dから離れているので損傷し難い。図中、1cは仕切り板、1bはインゴット投入室である。 In Figure 1, the distance d 1 between the melt surface of the lead melt 1d of the lower end and Namarikuzu turned chamber 1a of the opening 2a of the lead waste receptacle 2 below is preferable 50 mm. If d 1 is more than 50mm entrainment of the atmosphere by the flow落量of Namarikuzu molten metal, there is a case in which waving of the molten metal surface occurs. Here, the lead scrap container 2 is not easily damaged because it is separated from the molten lead 1d in the melting and holding furnace 1. In the figure, 1c is a partition plate and 1b is an ingot charging chamber.

本発明の鉛屑の溶解方法の他の実施形態では、図2に示すように、鉛屑受け容器2の底部を溶解保持炉1内の鉛溶湯1dに浸入させておくと、コンベアから落下する鉛屑4が、鉛屑受け容器2内の鉛溶湯に接触するので鉛屑4がより迅速に溶解し、生産性の向上およびエネルギーコストの低減が図れる。また鉛屑溶湯は開口部2aから鉛溶湯に1dに流出するだけで、流れ落ちないので鉛溶湯1dに大気の巻き込みや湯面の波立ちが起きることがない。図1と同じ符号は同じものを示す。   In another embodiment of the lead scrap melting method of the present invention, as shown in FIG. 2, if the bottom of the lead scrap receiving container 2 is allowed to enter the molten lead 1d in the melting and holding furnace 1, it falls from the conveyor. Since the lead scrap 4 comes into contact with the molten lead in the lead scrap receiving container 2, the lead scrap 4 is melted more quickly, and productivity can be improved and energy cost can be reduced. Further, the lead scrap molten metal only flows out into the lead molten metal 1d from the opening 2a, and does not flow down. Therefore, the lead molten metal 1d is not entrained in the atmosphere and the surface of the molten metal does not swell. The same reference numerals as those in FIG.

この際、鉛屑4が容器2内の鉛溶湯に直接落下しても、図3(イ)に示すように、大気の巻き込み、湯面の波立ちが鉛屑受け容器2内に制限され、更に還元炎5aが噴射されているのでドロスの発生が抑制される。
これに対し、従来の溶解方法では、図3(ロ)に示すように、鉛屑4がコンベアの高い位置から直接鉛溶湯1d内に落下するため大気の巻き込みや湯面の波立ちが広い範囲で起きる。
なお、鉛屑受け容器2の鉛溶湯1dの浸入深さ(開口部下端からの距離)は30mm以上がその効果が安定して現れ望ましい。
At this time, even if the lead scrap 4 falls directly on the molten lead in the container 2, as shown in FIG. 3 (a), the entrainment of the atmosphere and the undulation of the molten metal surface are limited in the lead scrap receiving container 2, Since the reducing flame 5a is injected, the generation of dross is suppressed.
On the other hand, in the conventional melting method, as shown in FIG. 3 (b), the lead scrap 4 falls directly into the molten lead 1d from a high position of the conveyor, so that the entrainment of the atmosphere and the undulation of the molten metal surface are within a wide range. Get up.
The penetration depth (distance from the lower end of the opening) of the lead molten metal 1d in the lead scrap receiving container 2 is preferably 30 mm or more because the effect is stable and desirable.

本発明において、「鉛屑の溶融体を溶解保持炉内の鉛溶湯中に静かに流入させる」とは、溶解保持炉内の鉛溶湯に大気が巻き込まれたり、鉛溶湯面が波立ったりしない状態で流入または流落させることを言う。具体的には、鉛屑受け容器の開口部を溶解保持炉内の鉛溶湯に十分近づける方法、鉛屑受け容器の底部を溶解保持炉内の鉛溶湯中に浸漬させる方法などにより行う。   In the present invention, the phrase “slowly flow the molten lead scrap into the molten lead in the melting and holding furnace” means that the atmosphere does not get involved in the molten lead in the melting and holding furnace, and the molten lead surface does not wave. Inflow or run down in a state. Specifically, it is performed by a method of sufficiently bringing the opening of the lead scrap receiving container close to the molten lead in the melting and holding furnace, a method of immersing the bottom of the lead scrap receiving container in the molten lead in the melting and holding furnace, and the like.

本発明において、鉛屑を加熱溶融するための還元炎には、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, the reducing flame for heating and melting the lead scrap includes controlling the air-fuel ratio of gas such as methane gas, ethane gas, propane gas, butane gas, city gas, etc., so that the CO concentration in the gas combustion flame is 0.5 to What was controlled to 5 mass% is applicable.

本発明において、鉛屑受け容器2には、図4(イ)に示す縦断面V字状の箱形のもの、同(ロ)に示す縦断面U字状の箱形のもの、同(ハ)に示す縦断面V字状の円錐形のものなどなど縦断面が凹状のものが使用できる。   In the present invention, the lead scrap receiving container 2 includes a box-shaped box having a V-shaped vertical section shown in FIG. 4 (a), a box-shaped box having a U-shaped vertical section shown in FIG. And those having a concave longitudinal section, such as a conical shape having a V-shaped longitudinal section shown in FIG.

本発明において、鉛屑受け容器の材料には、耐熱性を有し、かつ鉛溶湯に侵食され難い任意の材料が使用できるが、特に鉄板やステンレス板は溶解保持炉に合った形状に容易に形成できるので推奨される。鉛屑受け容器は、その鉛屑溶融体や鉛溶湯が接触する面に離型剤を塗付しておくと耐久性が向上する。   In the present invention, any material that has heat resistance and is not easily eroded by molten lead can be used as the material for the lead scrap receiving container. In particular, iron plates and stainless steel plates can be easily shaped to suit the melting and holding furnace. Recommended because it can be formed. The lead scrap receiving container is improved in durability if a release agent is applied to the surface with which the lead scrap melt or lead molten metal comes into contact.

本発明において、バーナーの本数は容器の大きさによって選定することが望ましい。容器が小さいときはバーナーの本数は1本でも良いが、容器が大きいときは、バーナーは複数本用いて容器内全体が還元性雰囲気で均一に加熱されるようにするのが望ましい。   In the present invention, the number of burners is preferably selected according to the size of the container. When the container is small, the number of burners may be one, but when the container is large, it is desirable to use a plurality of burners so that the entire interior of the container is uniformly heated in a reducing atmosphere.

本発明の鉛蓄電池用基板の製造方法を図5を参照して説明する。
溶解保持炉1内の鉛溶湯1dは、溶湯移送管6内を通って基板鋳造機7に導入されて格子基板が連続的に金型鋳造される。基板鋳造機7から排出された格子基板は直ちに不要部(図6に示した湯道部8aと湯底部8b)が切除されて次の極板工程に移送される。切除屑(鉛屑)4はコンベア3により移送され、溶解保持炉1の鉛屑投入室1a上に配された、縦断面が凹状で下部に開口部2aを有する鉛屑受け容器2内に落下する。前記容器2内に落下した鉛屑4は前述のように還元炎(図示せず)により表面の酸化膜が還元されつつ溶融し、開口部2aから溶解保持炉1の鉛溶湯1d中に流れ落ちて流入する。
The manufacturing method of the board | substrate for lead acid batteries of this invention is demonstrated with reference to FIG.
The molten lead 1d in the melting and holding furnace 1 is introduced into the substrate casting machine 7 through the molten metal transfer pipe 6, and the lattice substrate is continuously die-cast. The grid substrate discharged from the substrate casting machine 7 is immediately cut off unnecessary portions (runner portion 8a and bottom portion 8b shown in FIG. 6) and transferred to the next electrode plate process. The cutting waste (lead scrap) 4 is transferred by the conveyor 3 and dropped into the lead scrap receiving container 2 disposed on the lead scrap charging chamber 1a of the melting and holding furnace 1 and having a concave longitudinal section and an opening 2a at the bottom. To do. As described above, the lead scrap 4 that has fallen into the container 2 is melted while the oxide film on the surface is reduced by the reducing flame (not shown), and flows down from the opening 2a into the molten lead 1d of the melting and holding furnace 1. Inflow.

本発明は、内部が鉛屑投入室1aとインゴット投入室1bなどに仕切られていない溶解保持炉に適用しても同様の効果が得られる。   Even if the present invention is applied to a melting and holding furnace whose interior is not partitioned into a lead scrap charging chamber 1a and an ingot charging chamber 1b, the same effect can be obtained.

以下に本発明を実施例により具体的に説明する。   Hereinafter, the present invention will be described specifically by way of examples.

図5に示した本発明の製造装置を用いて鉛蓄電池用格子基板を製造した。鉛屑受け容器2には図4(イ)に示した縦断面V字状の箱形のものを用いた。
溶解保持炉1の鉛屑投入室1aの上部開口端の幅Wは600mm、長さTは600mmとした。鉛屑受け容器(SUS430製)2は、図4(イ)に示す様に、上端開口径Wは700mm、長さLは550mm、高さhは150mmとした。鉛屑受け容器2の底部には、幅20mm、長さ150mmの開口部2aを3個等間隔に設けた。鉛屑受け容器2の開口部2aの下端と鉛溶湯1d表面間の距離dは20±3mm、50±3mm、60±3mmの3通りに変化させた。鉛屑受け容器2の内外面にはドロスや溶湯が剥離し易いように離型剤(ボロンナイトライド粉)を塗布した。
A grid substrate for a lead storage battery was manufactured using the manufacturing apparatus of the present invention shown in FIG. As the lead scrap receiving container 2, a box-shaped one having a V-shaped longitudinal section shown in FIG.
The width W 1 of the upper open end of the Namarikuzu loading chamber 1a of the melting and holding furnace 1 is 600 mm, the length T 1 was 600 mm. Lead waste receptacle (manufactured by SUS430) 2 is, as shown in FIG. 4 (b), the upper end opening diameter W 2 700 mm, the length L is 550 mm, the height h 1 was 150 mm. Three openings 2a having a width of 20 mm and a length of 150 mm were provided at the bottom of the lead scrap receiving container 2 at equal intervals. The distance d 1 between the bottom and lead melt 1d the surface of the opening portion 2a of the lead waste receptacle 2 was changed to three types of 20 ± 3mm, 50 ± 3mm, 60 ± 3mm. A release agent (boron nitride powder) was applied to the inner and outer surfaces of the lead scrap receiving container 2 so that dross and molten metal were easily peeled off.

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た。鉛屑投入室1aの鉛溶湯は約500℃の温度に保持した。湯面のドロスは鋳造開始前に完全に除去した。鉛屑受け容器2内はバーナー5から放射されるプロパンガスの還元炎5aで充満させた。還元炎5aは開口部2aからも排出させ鉛屑投入室1aの湯面を覆うようにした。還元炎5a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。還元炎5aは青色を呈した。   About 2 tons of lead calcium alloy was melted in the melting and holding furnace 1. The molten lead in the lead scrap charging chamber 1a was kept at a temperature of about 500 ° C. The dross on the molten metal surface was completely removed before casting was started. The inside of the lead scrap receiving container 2 was filled with a reducing flame 5 a of propane gas radiated from the burner 5. The reducing flame 5a was also discharged from the opening 2a so as to cover the hot water surface of the lead scrap charging chamber 1a. The CO gas concentration of the reducing flame 5a was automatically controlled to 2-3% by adjusting the air-fuel ratio of the burner 8. The reducing flame 5a was blue.

次に、前記溶解保持炉1内の鉛溶湯1dを、ポンプ(図示せず)により溶湯移送管6内を通して2枚の金型からなるブックモールド鋳造機7に送り、格子基板8(図6参照)を鋳造した。鋳造したままの格子基板8は直ちに不要部8a、8bを切除し、不要部を切除した格子基板9は次の極板工程に移送した。切除した不要部(鉛屑4)はコンベア3により溶解保持炉1上に移送し、鉛屑受け容器2内に落下させた。落下した鉛屑4は鉛屑受け容器2内でバーナー5から噴射する高温の還元炎5aにより加熱され溶融して、鉛屑受け容器2の開口部2aから溶解保持炉1の鉛屑投入室1a内の鉛溶湯1d中に流れ落ちた。   Next, the molten lead 1d in the melting and holding furnace 1 is sent by a pump (not shown) through the molten metal transfer pipe 6 to the book mold casting machine 7 composed of two dies, and the lattice substrate 8 (see FIG. 6). ). The lattice substrate 8 as cast was immediately cut away from the unnecessary portions 8a and 8b, and the lattice substrate 9 cut away from the unnecessary portions was transferred to the next electrode plate process. The removed unnecessary part (lead scrap 4) was transferred onto the melting and holding furnace 1 by the conveyor 3 and dropped into the lead scrap receiving container 2. The fallen lead scrap 4 is heated and melted by the high-temperature reducing flame 5a sprayed from the burner 5 in the lead scrap receiving container 2, and the lead scrap input chamber 1a of the melting and holding furnace 1 from the opening 2a of the lead scrap receiving container 2 is melted. It flowed down into the molten lead 1d.

格子基板10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内の鉛溶湯1dの量は、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。インゴットは溶解保持炉に設置した湯面センサー(図示せず。)により湯面を検知し湯面が一定高さに維持されるように自動制御により投入した。切除屑4は1時間当たり100kg発生した。鉛屑投入室1aの湯面上に堆積したドロスは定期的に回収し、保管しておき、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 10 was cast at a rate of 17 sheets per minute for 5 hours. The amount of the molten lead 1d in the melting and holding furnace 1 was kept substantially constant (about 2 tons) by appropriately introducing a lead calcium alloy ingot. The ingot was introduced by automatic control so that the molten metal level was detected by a molten metal level sensor (not shown) installed in the melting and holding furnace and the molten metal level was maintained at a constant height. Excision waste 4 generated 100 kg per hour. The dross deposited on the molten metal surface of the lead scrap charging chamber 1a was periodically collected and stored, and after the completion of casting, all the collected dross was weighed. Moreover, the dross generation rate was calculated | required by remove | dividing the said total dross amount by the amount (500 kg) of the cutting waste returned to the melt | dissolution holding furnace.

図2に示すように鉛屑受け容器2を降下させ、その底部を鉛溶湯1bに浸入させた他は、実施例1と同じ方法により格子基板を製造し、実施例1と同じ調査を行った。なお鉛屑受け容器2の鉛溶湯1d内への浸入深さdは20±3mm、30±3mm、60±3mmの3通りに変化させた。 As shown in FIG. 2, the lattice substrate was manufactured by the same method as in Example 1 except that the lead scrap receiving container 2 was lowered and the bottom part was infiltrated into the molten lead 1 b, and the same investigation as in Example 1 was performed. . Note penetration depth d 2 of the lead scrap receptacle 2 of the lead melt 1d in was changed to three types of 20 ± 3mm, 30 ± 3mm, 60 ± 3mm.

[比較例1]
図7、8に示した従来の製造装置を用い、鉛屑4をコンベア3から溶解保持炉1の鉛屑投入室1aに直接落下させた他は、実施例1と同じ方法により格子基板を製造し、実施例1と同じ調査を行った。
[Comparative Example 1]
A grid substrate is manufactured by the same method as in Example 1 except that the lead scrap 4 is dropped directly from the conveyor 3 to the lead scrap input chamber 1a of the melting and holding furnace 1 using the conventional manufacturing apparatus shown in FIGS. The same investigation as in Example 1 was conducted.

実施例1、2よび比較例1の結果を表1に示す。   The results of Examples 1 and 2 and Comparative Example 1 are shown in Table 1.

表1から明らかなように、本発明例の実施例1ではドロス発生率が比較例1(従来法)に比べて大幅に低下した。これは、実施例1では、鉛屑受け容器を用いて鉛屑(切除屑)を、その表面の酸化物を還元炎を照射して除去しつつ溶融し、この鉛屑の溶融体を溶解保持炉内の鉛溶湯中に近距離から静かに流落させたことによる。流落距離dを50mm以下とすることによりにドロス発生率が大幅に低下した。 As is apparent from Table 1, the dross generation rate in Example 1 of the present invention example was significantly lower than that in Comparative Example 1 (conventional method). In the first embodiment, the lead scrap (cutting scrap) is melted by removing the oxide on the surface by irradiating the reducing flame using a lead scrap receiving container, and the melt of the lead scrap is dissolved and held. This is because it was gently poured into the molten lead in the furnace from a short distance. Dross incidence was decreased significantly by the Nagare落distance d 1 and 50mm or less.

実施例2では鉛屑受け容器底部を溶解保持炉内の鉛溶湯に浸入させたので大気の巻き込みや湯面の波立ちは全く起きず、ドロスの発生率は1.06%以下に低下した。浸入深さdを30mm以上とすることによりドロス発生率は大幅に低下した。 In Example 2, since the bottom part of the lead scrap receiving container was infiltrated into the molten lead in the melting and holding furnace, the entrainment of the atmosphere and the undulation of the molten metal surface did not occur at all, and the dross generation rate decreased to 1.06% or less. Dross generation rate by the penetration depth d 2 and 30mm or more were significantly reduced.

上記実施例では、図4(イ)に示した鉛屑受け容器(SUS製)を用い、鉛屑をプロパンガスを用いて溶融する場合について説明したが、別途行った実験により、図4(ロ)、(ハ)に示すような他の鉛屑受け容器を用いても、またブタンガス、都市ガスなど他のガスを用いても同様の効果が得られることを確認した。   In the above embodiment, the lead scrap receiving container (manufactured by SUS) shown in FIG. 4 (a) is used and lead scrap is melted using propane gas. ) And (c), it was confirmed that the same effect can be obtained by using other lead scrap receptacles as shown in (c) or using other gases such as butane gas and city gas.

本発明の鉛屑の溶解方法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 melting method of the lead scrap of this invention. 本発明の鉛屑の溶解方法の他の実施形態を示す側面説明図である。It is side explanatory drawing which shows other embodiment of the melt | dissolution method of the lead scrap of this invention. 鉛屑投入時の鉛溶湯の動きを示す側面説明図で、(イ)は本発明方法の場合、(ロ)は従来方法の場合である。It is side surface explanatory drawing which shows the motion of the lead molten metal at the time of lead waste injection | throwing-in, (A) is a case of this invention method, (B) is a case of a conventional method. (イ)〜(ハ)は本発明で用いる鉛屑受け容器の実施形態を示すそれぞれ平面図およびA−A断面図(縦断面図)である。(A)-(C) are respectively a plan view and an AA sectional view (longitudinal sectional view) showing an embodiment of a lead scrap receiving container used in the present invention. 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. (イ)は鋳造したままの格子基板の正面図、(ロ)は不要部を切除したあとの格子基板の正面図である。(A) is a front view of the lattice substrate as cast, and (B) is a front view of the lattice substrate after unnecessary portions are cut away. 従来の鉛蓄電池用基板の製造装置の平面説明図である。It is plane explanatory drawing of the manufacturing apparatus of the conventional board | substrate for lead acid batteries. 図7に示した製造装置の溶解保持炉部分の側面説明図である。It is side surface explanatory drawing of the melt | dissolution holding furnace part of the manufacturing apparatus shown in FIG.

符号の説明Explanation of symbols

1 溶解保持炉
1a 鉛屑投入室
1b インゴット投入室
1c 仕切板
1d 鉛溶湯
2 鉛屑受け容器
2a 鉛屑受け容器の底部の開口部
3 コンベア
4 鉛屑
5 バーナー
5a 還元炎
6 溶湯移送管
7 基板鋳造機
8 鋳造したままの格子基板
8a 湯道部(不要部)
8b 湯底部(不要部)
9 不要部を除去したあとの格子基版(鉛蓄電池用基板)
DESCRIPTION OF SYMBOLS 1 Melting and holding furnace 1a Lead scrap input chamber 1b Ingot input chamber 1c Partition plate 1d Lead molten metal 2 Lead scrap receiving container 2a Opening part of bottom part of lead scrap receiving container 3 Conveyor 4 Lead scrap 5 Burner 5a Reduction flame 6 Molten metal transfer pipe 7 Substrate Casting machine 8 As-cast grid substrate 8a Runway (unnecessary part)
8b Hot water bottom (unnecessary part)
9 Lattice base plate after removing unnecessary parts (Lead storage battery substrate)

Claims (6)

鉛または鉛合金溶解保持炉上に縦断面が凹状で底部に開口部を有する鉛屑受け容器を配し、前記鉛屑受け容器内に鉛屑を供給し、前記鉛屑を還元炎で加熱溶融し、この鉛屑の溶融体を前記鉛屑受け容器の開口部から溶解保持炉内の鉛または鉛合金溶湯中に静かに流入させることを特徴とする鉛屑の溶解方法。   A lead scrap receiving container having a concave longitudinal section and having an opening at the bottom is arranged on a lead or lead alloy melting and holding furnace, the lead scrap is supplied into the lead scrap receiving container, and the lead scrap is heated and melted with a reducing flame. A lead scrap melting method is characterized in that the molten lead scrap is gently allowed to flow into the lead or molten lead alloy in the melting and holding furnace from the opening of the lead scrap receiving container. 前記鉛屑受け容器の底部を溶解保持炉内の鉛または鉛合金溶湯中に浸入させることを特徴とする請求項1に記載の鉛屑の溶解方法。   The method for melting lead scraps according to claim 1, wherein the bottom of the lead scrap receiving container is allowed to enter a lead or lead alloy molten metal in a melting and holding furnace. 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を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、前記溶解保持炉上に配した縦断面が凹状で底部に開口部を有する鉛屑受け容器内に供給し、前記鉛屑を還元炎で加熱溶融し、この鉛屑の溶融体を前記鉛屑受け容器の開口部から溶解保持炉内の鉛または鉛合金溶湯中に静かに流入させる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 storage battery substrate in which a lattice substrate is cast by a substrate casting machine using molten lead or lead alloy molten metal in a melting holding furnace, lead scraps generated in the substrate casting machine are arranged on the melting holding furnace. The lead scrap is received in a lead scrap receiving container having a concave surface and an opening at the bottom, and the lead scrap is heated and melted with a reducing flame, and the melt of the lead scrap is melted into the melting and holding furnace from the opening of the lead scrap receiving container. A method for producing a lead-acid battery substrate, wherein the lead-acid battery is gently allowed to flow into a molten lead or lead alloy. 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装置において、前記溶解保持炉上に、縦断面が凹状で底部に開口部を有する鉛屑受け容器および前記鉛屑受け容器内の鉛屑を還元炎で加熱溶融するためのバーナー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 storage battery substrate manufacturing apparatus for casting lead or lead alloy melt melted in a melting and holding furnace to a lattice substrate by a substrate casting machine, lead scrap having a concave longitudinal section and an opening at the bottom on the melting and holding furnace An apparatus for producing a lead-acid battery substrate, comprising a receiving container and a burner for heating and melting lead scrap in the lead scrap receiving container with a reducing flame. 前記鉛屑受け容器が鉄系またはステンレス系の金属材料で構成されていることを特徴とする請求項4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 claim 4, wherein the lead scrap receiving container is made of an iron-based or stainless-based metal material. バーナーが2基以上備えられていることを特徴とする請求項4または5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 claim 4 or 5, wherein two or more burners are provided.
JP2007169645A 2007-06-27 2007-06-27 Method for melting lead scrap, and method for manufacturing substrate for lead battery and manufacturing method thereof Pending JP2009007622A (en)

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JPS5228403A (en) * 1975-08-29 1977-03-03 Fuaanesu Kakoki Kk Melting and holding method
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
JPH0845565A (en) * 1994-07-28 1996-02-16 Shin Kobe Electric Mach Co Ltd Melting device for plate and plate group of lead storage battery
JPH11246920A (en) * 1998-03-05 1999-09-14 Osaka Namarisuzu Seirensho:Kk Lead smelting furnace and method for smelting lead
JP2000129366A (en) * 1998-10-23 2000-05-09 Nippon Senzai Kk Method for melting non-ferrous metal and apparatus used for this method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5228403A (en) * 1975-08-29 1977-03-03 Fuaanesu Kakoki Kk Melting and holding method
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
JPH0845565A (en) * 1994-07-28 1996-02-16 Shin Kobe Electric Mach Co Ltd Melting device for plate and plate group of lead storage battery
JPH11246920A (en) * 1998-03-05 1999-09-14 Osaka Namarisuzu Seirensho:Kk Lead smelting furnace and method for smelting lead
JP2000129366A (en) * 1998-10-23 2000-05-09 Nippon Senzai Kk Method for melting non-ferrous metal and apparatus used for this method

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