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JPH0845565A - Dissolution device for electrode plates and electrode plates of lead acid batteries - Google Patents

Dissolution device for electrode plates and electrode plates of lead acid batteries

Info

Publication number
JPH0845565A
JPH0845565A JP17671394A JP17671394A JPH0845565A JP H0845565 A JPH0845565 A JP H0845565A JP 17671394 A JP17671394 A JP 17671394A JP 17671394 A JP17671394 A JP 17671394A JP H0845565 A JPH0845565 A JP H0845565A
Authority
JP
Japan
Prior art keywords
melting
plate
electrode plate
lead alloy
melted
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
JP17671394A
Other languages
Japanese (ja)
Inventor
Takayuki Arai
孝之 新井
Takeshi Hirakawa
武 平川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP17671394A priority Critical patent/JPH0845565A/en
Publication of JPH0845565A publication Critical patent/JPH0845565A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • 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

Landscapes

  • Secondary Cells (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

(57)【要約】 【目的】 廃板,廃板群からの鉛合金の回収率を増加さ
せ、発生する廃棄物量を削減できる極板,極板群の溶解
装置を提供する。 【構成】 溶解炉1内の上部に極板又は極板群のいずれ
か一方又は双方からなる被溶解物6を投入する被溶解物
投入部屋13を設け、溶解炉1内の下部には被溶解物6
を熱溶解して得られた溶解鉛合金7を回収する溶解鉛合
金回収部屋14を設ける。両部屋13,14の間は被溶
解物6を加熱して溶解させると共に得られた溶解鉛合金
7を孔15aから落として分離する有孔分離板15で仕
切る。
(57) [Summary] [Objective] To provide an electrode plate / electrode plate melting apparatus capable of increasing the recovery rate of lead alloys from waste plates and waste plate groups and reducing the amount of waste generated. [Configuration] A melted material charging chamber 13 for charging a melted material 6 composed of one or both of an electrode plate and an electrode plate group is provided in the upper portion of the melting furnace 1, and a material to be melted is provided in a lower portion of the melting furnace 1. Thing 6
A molten lead alloy recovery chamber 14 for recovering the molten lead alloy 7 obtained by heat-melting is prepared. The space between the chambers 13 and 14 is partitioned by a perforated separation plate 15 which separates the melted lead alloy 7 obtained by heating and melting the melted material 6 by dropping it from the holes 15a.

Description

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

【0001】本発明は、鉛蓄電池の極板,極板群を熱溶
解して再利用するための鉛蓄電池の極板,極板群の溶解
装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrode plate of a lead storage battery and a melting device of the electrode plate group for thermally melting and reusing the electrode plate and electrode plate group of the lead storage battery.

【0002】[0002]

【従来の技術】従来、鉛蓄電池の極板,極板群を再利用
する方法は、溶解炉を用いた熱溶解法が一般的であっ
た。これは、鉛蓄電池の製造工程で不良となって廃棄さ
れた未化成の極板又は極板群のいずれか一方又は双方か
らなる被溶解物を熱溶解して合金部分(格子体,ストラ
ップ,極柱)を回収し、故鉛として再利用する手法であ
る。
2. Description of the Related Art Conventionally, a thermal melting method using a melting furnace has been generally used as a method of reusing an electrode plate or a group of electrode plates of a lead storage battery. This is because the melted material consisting of either or both of the unformed electrode plate or electrode plate group that has been discarded due to a defect in the lead-acid battery manufacturing process is thermally melted and the alloy portion (lattice, strap, electrode) is melted. It is a method to collect pillars and reuse them as lead.

【0003】鉛蓄電池の組立工程で不良となった未化成
の極板からなる廃板は、一酸化鉛(PbO)を主成分と
する未化成活物質と該未化成活物質を保持するPb−S
b系又はPb−Ca系の格子体とで構成されている。一
方、未化成の極板群からなる廃板群は、複数の廃板と耳
の部分をPb−Sb系のストラップ及び極柱で群溶接し
たものである。
A waste plate consisting of an unformed electrode plate which has become defective in the process of assembling a lead-acid battery is an unactivated material containing lead monoxide (PbO) as a main component and Pb-containing the unactivated material. S
It is composed of a b-based or Pb-Ca-based lattice. On the other hand, a waste plate group consisting of unformed electrode plates is a group of a plurality of waste plates and ears that are group-welded with a Pb-Sb system strap and a pole.

【0004】従来の廃板,廃板群からなる被溶解物を熱
溶解して格子体,ストラップ,極柱からなる鉛合金を回
収する極板,極板群の溶解装置の構成を図5(A)〜
(E)を参照して説明する。図5(A)は従来の極板,
極板群の溶解装置における平面図を示し、図5(B)〜
(E)は図5(A)のY−Y線断面図を示す。図におい
て、1は溶解炉、1aは溶解炉1の上部に設けられた
扉、2は溶解炉1の溶解室3における底板、4は底板2
の下に設けられている重油バーナ、5は重油バーナ4の
加熱により得られた溶解浴、6は溶解室3に投入された
廃板,廃板群からなる被溶解物、7は廃板,廃板群から
なる被溶解物6が溶解して得られた溶解鉛合金、8は溶
解浴5上に浮いた活物質及び未溶解合金、9は溶解炉1
の側壁を貫通して設けられたポンプ、10はポンプ9の
吸上げパイプ、11はポンプ9の吐出パイプ、12は吐
出パイプ11の下に配置された回収缶である。
FIG. 5 shows the structure of a conventional electrode plate and an electrode plate melting device for recovering a lead alloy composed of a grid, a strap, and a pole by thermally melting a material to be melted composed of a waste plate and a waste plate group. A) ~
This will be described with reference to (E). FIG. 5A shows a conventional electrode plate,
FIG. 5B shows a plan view of the melting device for the electrode plate group.
(E) shows the YY sectional view taken on the line of FIG. 5 (A). In the figure, 1 is a melting furnace, 1 a is a door provided above the melting furnace 1, 2 is a bottom plate in a melting chamber 3 of the melting furnace 1, and 4 is a bottom plate 2.
5, a heavy oil burner provided underneath, 5 is a melting bath obtained by heating the heavy oil burner 4, 6 is a waste plate put into the melting chamber 3, a substance to be melted consisting of a waste plate group, 7 is a waste plate, A molten lead alloy obtained by melting a material 6 to be melted composed of a waste plate group, 8 is an active material and an unmelted alloy floating on a melting bath 5, and 9 is a melting furnace 1.
A pump provided through the side wall of the pump, 10 is a suction pipe of the pump 9, 11 is a discharge pipe of the pump 9, and 12 is a recovery can disposed under the discharge pipe 11.

【0005】次に、このような極板,極板群の溶解装置
の動作について説明する。図5(b)に示すように予め
Pb−Sb系の故鉛を溶解し凝固させ、溶解室3の底部
に溶解浴5を形成する。次に、図5(c)に示すように
溶解炉1に扉1aを開けて廃板,廃板群からなる被溶解
物6を投入し、重油バーナ4で加熱して溶解浴5上で廃
板,廃板群からなる被溶解物6を溶解する。溶解浴5の
温度が480 〜500 ℃になった時点で廃板,廃板群からな
る被溶解物6を粉砕、攪拌し、図5(d)の状態にす
る。廃板,廃板群からなる被溶解物6が溶解されて得ら
れた溶解鉛合金7は流動性があり、活物質より比重が大
きいので、活物質の間隙を通って溶解浴5に溶解する。
そして、予め溶解浴5中に導入しておいた吸上げパイプ
10からポンプ9の吸上げによって図5(e)に示すよ
うに溶解浴5及び溶解鉛合金7を回収缶12に回収す
る。その後、溶解浴5上に浮いた活物質及び未溶解合金
8を採取し、同様の操作を繰り返す。活物質及び未溶解
合金8は廃棄物として別途処理する。
Next, the operation of the melting device for such an electrode plate or electrode plate group will be described. As shown in FIG. 5 (b), the Pb—Sb system lead is previously dissolved and solidified to form a dissolution bath 5 at the bottom of the dissolution chamber 3. Next, as shown in FIG. 5 (c), the door 1 a is opened in the melting furnace 1 and the material 6 to be melted consisting of a waste plate and a waste plate group is charged and heated by the heavy oil burner 4 to waste on the melting bath 5. The material 6 to be melted, which consists of plates and waste plates, is melted. When the temperature of the melting bath 5 reaches 480 to 500 ° C., the material 6 to be melted consisting of a waste plate and a waste plate group is crushed and stirred to obtain the state of FIG. 5 (d). The molten lead alloy 7 obtained by melting the material 6 to be melted composed of the waste plate and the waste plate group has fluidity and has a larger specific gravity than the active material, and therefore melts in the melting bath 5 through the gap of the active material. .
Then, as shown in FIG. 5E, the melting bath 5 and the molten lead alloy 7 are collected in the collecting can 12 by suction of the pump 9 from the suction pipe 10 previously introduced into the melting bath 5. Then, the active material and the undissolved alloy 8 floating on the dissolution bath 5 are collected, and the same operation is repeated. The active material and the unmelted alloy 8 are separately treated as waste.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、このよ
うな従来の鉛蓄電池の極板,極板群の溶解装置では、重
油バーナ4で加熱する際に熱が伝達し易い溶解浴5が最
初に溶解し、その後に廃板,廃板群からなる被溶解物6
が溶解するため溶解に時間がかかり、その結果、活物質
を保持している格子体の鉛合金が酸化され、溶解浴5中
に溶け込まず、活物質に付着して溶解浴5上に浮かぶた
めに、廃板及び廃板群からの鉛合金の回収率が3割前後
に留まっていた。そのため、廃棄物として別途処理する
活物質及び未溶解合金が多量に発生するという問題点が
あった。
However, in such a conventional apparatus for dissolving an electrode plate or an electrode plate group of a lead storage battery, when the heavy oil burner 4 is used for heating, the dissolution bath 5 to which heat is easily transferred is first melted. Then, the melted material 6 consisting of waste plate and waste plate group 6
Since it takes a long time to dissolve, the lead alloy of the lattice holding the active material is oxidized and does not melt into the melting bath 5, but adheres to the active material and floats on the melting bath 5. Moreover, the recovery rate of the lead alloy from the waste plate and the waste plate group remained around 30%. Therefore, there is a problem in that a large amount of active material and unmelted alloy that are separately treated as waste are generated.

【0007】本発明の目的は、廃板,廃板群からの鉛合
金の回収率を増加させ、発生する廃棄物量を削減できる
極板,極板群の溶解装置を提供することにある。
It is an object of the present invention to provide an electrode plate / electrode plate melting apparatus capable of increasing the recovery rate of a lead alloy from a waste plate / waste plate group and reducing the amount of waste generated.

【0008】[0008]

【課題を解決するための手段】本発明に係る鉛蓄電池の
極板,極板群の溶解装置は、溶解炉内の上部に極板又は
極板群のいずれか一方又は双方からなる被溶解物を投入
する被溶解物投入部屋が設けられ、前記溶解炉内の下部
には前記被溶解物を熱溶解して得られた溶解鉛合金を回
収する溶解鉛合金回収部屋が設けられ、前記両部屋の間
は前記被溶解物を加熱して溶解させると共に得られた溶
解鉛合金を孔から落として分離する有孔分離板で仕切ら
れていることを特徴とする。
DISCLOSURE OF THE INVENTION A melting apparatus for a lead plate and an electrode group of a lead storage battery according to the present invention comprises an electrode plate or an electrode plate group, or an object to be melted, which is formed in an upper portion of a melting furnace. A melted material charging chamber for charging the melted lead alloy is provided in a lower portion of the melting furnace, and a melted lead alloy recovery room for recovering a melted lead alloy obtained by thermally melting the melted material is provided in both chambers. The space between the two is characterized by being divided by a perforated separation plate that heats and melts the material to be melted and drops the obtained molten lead alloy from the holes for separation.

【0009】この場合、前記有孔分離板の孔の大きさ
は、0.7 〜3.8 mmであることが好ましい。
In this case, the size of the holes of the perforated separation plate is preferably 0.7 to 3.8 mm.

【0010】また溶解炉には、前記溶解鉛合金回収部屋
の下部に溶解鉛合金回収穴を設けることが好ましい。
In the melting furnace, it is preferable to provide a molten lead alloy recovery hole under the molten lead alloy recovery chamber.

【0011】また前記有孔分離板は、溶解炉の外に配置
した電熱ヒータ又は誘導加熱コイルで加熱することがで
きる。
Further, the perforated separation plate can be heated by an electric heater or an induction heating coil arranged outside the melting furnace.

【0012】また前記有孔分離板は、内蔵する電熱ヒー
タで加熱することができる。
Further, the perforated separation plate can be heated by a built-in electric heater.

【0013】[0013]

【作用】このように溶解炉内に有孔分離板を配置し、そ
の上に極板,極板群からなる被溶解物を載せ、該被溶解
物を有孔分離板で直接加熱すると、格子体の溶解が速や
かに起こり、酸化して活物質に付着する鉛合金量が減少
する。更に、活物質のみが有孔分離板上に堆積し、溶解
鉛合金が該有孔分離板の孔を通り抜けて下の溶解鉛合金
回収部屋に落下して溶解部分と不溶解部分の分離が容易
になる。以上のような作用によって、本発明では鉛合金
の回収率が増加する。
In this way, the perforated separation plate is arranged in the melting furnace, the material to be melted consisting of the electrode plate and the electrode plate group is placed thereon, and the material to be melted is directly heated by the perforated separation plate. Dissolution of the body occurs rapidly, and the amount of lead alloy that oxidizes and adheres to the active material decreases. Furthermore, only the active material is deposited on the perforated separation plate, and the molten lead alloy passes through the holes of the perforated separation plate and falls into the molten lead alloy recovery chamber below, facilitating the separation of the melted portion and the insoluble portion. become. According to the present invention, the lead alloy recovery rate increases due to the above-described actions.

【0014】この場合、有孔分離板の孔の大きさが3.8
mmより大きいと、該有孔分離板の孔から活物質も落下し
て溶解鉛合金の中に混入されていまい好ましくない。有
孔分離板の孔の大きさが0.7 mmより小さいと、溶解鉛合
金が有孔分離板の孔から通り抜け難くなるため好ましく
ない。
In this case, the hole size of the perforated separation plate is 3.8.
If it is larger than mm, the active material may fall from the holes of the perforated separation plate and be mixed in the molten lead alloy, which is not preferable. If the hole size of the perforated separation plate is smaller than 0.7 mm, the molten lead alloy is difficult to pass through the holes of the perforated separation plate, which is not preferable.

【0015】溶解鉛合金回収部屋の下部に溶解鉛合金回
収穴を設けると、溶解炉からの溶解鉛合金の回収が容易
となる。
If a molten lead alloy recovery hole is provided in the lower portion of the molten lead alloy recovery chamber, recovery of the molten lead alloy from the melting furnace becomes easy.

【0016】[0016]

【実施例】図1(A)〜(C)は、本発明に係る鉛蓄電
池の極板,極板群の溶解装置における一実施例を示した
ものである。図1(A)は本実施例の溶解装置における
平面図を示し、図1(B)(C)は図1(A)のX−X
線断面図を示す。図において、1はステンレススチール
等で形成された溶解炉、1aは溶解炉1の上部に設けら
れた扉、13は溶解炉1内の上部に未完成の極板又は極
板群のいずれか一方又は双方からなる被溶解物6を投入
するために設けられた被溶解物投入部屋、14は溶解炉
1内の下部に被溶解物6を熱溶解して得られた溶解鉛合
金7を回収するために設けられた溶解鉛合金回収部屋、
15は被溶解物6を加熱して溶解させると共に得られた
溶解鉛合金7を孔15aから落として分離するために両
部屋13,14を間を仕切って設けられた有孔分離板、
16は溶解炉1の外周に配置されて有孔分離板15を加
熱する電熱ヒータ、17は溶解鉛合金回収部屋14の下
で溶解炉1に設けられた溶解鉛合金回収穴である。溶解
鉛合金回収穴17の下には、回収缶12が配置されてい
る。溶解炉1はその底部1bが漏斗状のテーパ形に形成
され、このテーパ形の底部1bの末端に溶解鉛合金回収
穴17が設けられている。
1 (A) to 1 (C) show an embodiment of a melting device for a plate and a plate group of a lead storage battery according to the present invention. FIG. 1 (A) shows a plan view of the melting apparatus of this embodiment, and FIGS. 1 (B) and 1 (C) are XX of FIG. 1 (A).
A line sectional view is shown. In the figure, 1 is a melting furnace formed of stainless steel or the like, 1a is a door provided on the upper part of the melting furnace 1, and 13 is either an unfinished electrode plate or an electrode plate group in the upper part of the melting furnace 1. Alternatively, a melted substance charging chamber provided for charging the melted substance 6 composed of both of them, and 14 collects the molten lead alloy 7 obtained by thermally melting the melted substance 6 in the lower portion of the melting furnace 1. A molten lead alloy recovery room,
Reference numeral 15 denotes a perforated separation plate provided by partitioning both chambers 13 and 14 in order to heat and melt the material 6 to be melted and drop the obtained molten lead alloy 7 from the hole 15a.
Reference numeral 16 denotes an electric heater which is arranged on the outer periphery of the melting furnace 1 and heats the perforated separation plate 15. Reference numeral 17 denotes a molten lead alloy recovery hole provided in the melting furnace 1 under the molten lead alloy recovery chamber 14. Below the molten lead alloy recovery hole 17, the recovery can 12 is arranged. The melting furnace 1 has a bottom 1b formed in a funnel-shaped tapered shape, and a molten lead alloy recovery hole 17 is provided at the end of the tapered bottom 1b.

【0017】本実施例では、溶解炉1はその内径が250
mm、上端から溶解鉛合金回収穴17までの深さが250 mm
となっている。有孔分離板15は、構造用鋼SS41で
形成されている。なお、有孔分離板15の材質は、溶解
鉛合金7と反応しない、溶解すべき極板,極板群からな
る被溶解物6を保持する強度を有するという条件を具備
していれば特に制約されない。有孔分離板15の孔15
aの大きさは、2.0 mmとした。溶解炉1の底部1bの勾
配の角度は、鉛直方向に対して120 °とした。溶解鉛合
金回収穴17の内径は30 mm とした。溶解炉1の外周に
配置した電熱ヒータ16は、できるだけ有孔分離板15
の近傍に配置した。
In this embodiment, the melting furnace 1 has an inner diameter of 250
mm, the depth from the upper end to the molten lead alloy recovery hole 17 is 250 mm
Has become. The perforated separation plate 15 is made of structural steel SS41. It should be noted that the material of the perforated separation plate 15 is particularly limited as long as it has a condition that it does not react with the molten lead alloy 7 and has a strength for holding the material to be melted 6 composed of the electrode plate and the electrode plate group to be melted. Not done. Hole 15 of perforated separation plate 15
The size of a was 2.0 mm. The angle of inclination of the bottom portion 1b of the melting furnace 1 was 120 ° with respect to the vertical direction. The inner diameter of the molten lead alloy recovery hole 17 was 30 mm. The electric heater 16 arranged on the outer periphery of the melting furnace 1 has a perforated separation plate 15 as far as possible.
It was placed in the vicinity of.

【0018】次に、このような極板,極板群の溶解装置
の動作について説明する。扉1aを開けて溶解炉1内
に、図1(B)に示すように格子体がPb−Ca系の廃
板,廃板群からなる被溶解物6を50 Kg 投入し、電熱ヒ
ータ16に通電して有孔分離板15を加熱した。有孔分
離板15の温度は500 ±10℃に制御した。有孔分離板1
5の温度上昇に伴い、廃板,廃板群からなる被溶解物6
から格子体,ストラップ及び極柱の部分が溶解する。こ
の溶解により得られた溶解鉛合金7は流動性があり、活
物質より比重が大きいので、活物質の間隙と有孔分離板
15の孔15aを通って図1(C)に示すように溶解鉛
合金回収部屋14に落下する。溶解鉛合金7は溶解炉1
の底部1bの勾配に沿って溶解鉛合金回収穴17に流
れ、回収缶12に回収される。更に、溶解鉛合金7を流
れ易くするために、廃板,廃板群からなる被溶解物6を
粉砕、攪拌する。有孔分離板15上に残った活物質及び
未溶解合金8は扉1aを開けて水平方向へかきだして回
収する。そのため扉1aの下端と有孔分離板15は水平
に配置した。溶解炉1内に残った活物質を圧縮空気等で
除去した後、また同様の操作を繰り返す。この場合、溶
解炉1も電熱ヒータ16や図示しない補助ヒータで加熱
しておくと、有孔分離板15から落下する溶解鉛合金7
が硬化するのを防止できる。
Next, the operation of the melting device for such an electrode plate or electrode plate group will be described. As shown in FIG. 1 (B), the door 1a is opened and 50 Kg of the melted material 6 consisting of a waste plate or a waste plate group having a lattice of Pb-Ca system is put into the melting furnace 1 and the electric heater 16 is charged. The perforated separation plate 15 was heated by applying electricity. The temperature of the perforated separation plate 15 was controlled to 500 ± 10 ° C. Perforated separation plate 1
With the temperature rise of 5, the melted material consisting of waste plates and waste plates 6
The grid, straps, and poles are melted from. Since the molten lead alloy 7 obtained by this melting has fluidity and has a larger specific gravity than the active material, it melts through the gap of the active material and the hole 15a of the perforated separation plate 15 as shown in FIG. 1 (C). It falls into the lead alloy recovery room 14. Molten lead alloy 7 is melting furnace 1
It flows into the molten lead alloy recovery hole 17 along the gradient of the bottom portion 1b of and is recovered in the recovery can 12. Further, in order to facilitate the flow of the molten lead alloy 7, the material 6 to be melted composed of a waste plate and a waste plate group is crushed and stirred. The active material and the undissolved alloy 8 remaining on the perforated separation plate 15 are recovered by opening the door 1a and horizontally scraping. Therefore, the lower end of the door 1a and the perforated separation plate 15 are arranged horizontally. After removing the active material remaining in the melting furnace 1 with compressed air or the like, the same operation is repeated. In this case, when the melting furnace 1 is also heated by the electric heater 16 or an auxiliary heater (not shown), the molten lead alloy 7 falling from the perforated separation plate 15
Can be prevented from hardening.

【0019】表1は、従来の極板,極板群の溶解装置
(従来装置という)と本発明に係る極板,極板群の溶解
装置(本発明装置という)の鉛合金の回収率を比較した
結果を示す。なお、試験回数は5回である。
Table 1 shows the recovery rates of lead alloys in the conventional electrode plate / electrode plate melting device (referred to as a conventional device) and the electrode plates and electrode plate melting device according to the present invention (referred to as the present invention device). The result of comparison is shown. The number of tests is 5.

【0020】従来装置の回収率は、式1によった。The recovery rate of the conventional device is based on the equation (1).

【0021】[式1] 回収率(%)=(投入した廃板,廃板群からなる被溶解
物6の重量−回収した活物質及び未溶解合金8の重量)
/(投入した廃板,廃板群からなる被溶解物6の鉛合金
の重量)×100 本発明装置の回収率は、式2によった。
[Equation 1] Recovery rate (%) = (weight of thrown waste plate, material 6 to be melted consisting of waste plate-weight of recovered active material and undissolved alloy 8)
/ (Weight of lead alloy of melted material 6 consisting of waste plate and waste plate group) × 100 The recovery rate of the device of the present invention was calculated by Equation 2.

【0022】[式2] 回収率(%)=(回収した溶解鉛合金7の重量)/(投
入した廃板,廃板群からなる被溶解物6の鉛合金の重
量)×100
[Equation 2] Recovery rate (%) = (weight of recovered molten lead alloy 7) / (weight of lead alloy of melted material 6 consisting of input waste plate and waste plate group) × 100

【表1】 これより、本発明装置は既述のように直接溶解する有孔
分離板15を用いたため、格子体の溶解が速やかに起こ
り、酸化した活物質に付着する量が減少し、溶解部分と
不溶解部分の分離が容易になるため、従来装置に比べ鉛
合金の回収率が大幅に増加した。
[Table 1] From this, since the device of the present invention uses the perforated separation plate 15 that directly dissolves as described above, dissolution of the lattice body occurs promptly, the amount adhering to the oxidized active material decreases, and the dissolved portion and insoluble matter Since the parts can be separated easily, the recovery rate of the lead alloy is significantly increased compared to the conventional device.

【0023】図2は、有孔分離板15の孔15aの大き
さを変えた場合の鉛合金の回収率の変化を示す図であ
る。数値は5回の試験の最高値である。
FIG. 2 is a diagram showing changes in the recovery rate of the lead alloy when the size of the holes 15a of the perforated separation plate 15 is changed. Numbers are the highest of 5 tests.

【0024】有孔分離板15の孔15aの大きさが1.0
mm以下で、急激に鉛合金の回収率が低下するのは、溶解
鉛合金7の表面張力のために有孔分離板15の孔15a
から該溶解鉛合金7が流れ落ち難くくなるためである。
また、有孔分離板15の孔15aが大きくなると、該孔
15aの間から活物質も落下して溶解鉛合金7中に混入
する。活物質を溶解鉛合金7から採取して分離するた
め、有孔分離板15の孔15aが大きくなっても鉛合金
の回収率が低下する。故に、有孔分離板15の孔15a
の大きさは、従来装置の回収率を上回る0.7 〜3.8 mmが
よいことが分かる。
The size of the hole 15a of the perforated separation plate 15 is 1.0.
The recovery rate of the lead alloy sharply decreases in the range of mm or less because the surface tension of the molten lead alloy 7 causes the holes 15a of the perforated separation plate 15 to be separated.
This is because the molten lead alloy 7 becomes difficult to flow down.
Further, when the hole 15a of the perforated separation plate 15 becomes large, the active material also falls from between the holes 15a and mixes in the molten lead alloy 7. Since the active material is collected from the molten lead alloy 7 and separated, even if the hole 15a of the perforated separation plate 15 becomes large, the lead alloy recovery rate decreases. Therefore, the hole 15a of the perforated separation plate 15
It can be seen that the size of is better than the recovery rate of the conventional device, 0.7-3.8 mm.

【0025】本実施例では、有孔分離板15の加熱方式
として、溶解炉1に外付けの電熱ヒータ16を用いた
が、図3に示すように有孔分離板15の格子又は網の線
の全部または一部を線状,棒状のシーズヒータ15bに
置き換えたり、図4に示すように溶解炉1の外周に誘導
加熱コイル18を配置しても同様の効果が得られた。誘
導加熱コイル18を用いる場合には、例えば溶解炉1は
セラミックの如き非磁性材で形成し、有孔分離板15は
前述したように構造用鋼SS41で形成する。
In this embodiment, as the heating method for the perforated separation plate 15, an external electric heater 16 is used in the melting furnace 1. However, as shown in FIG. 3, a grid or mesh line of the perforated separation plate 15 is used. The same effect was obtained by replacing all or part of the sheath heater 15b with a linear or rod shape or disposing the induction heating coil 18 on the outer periphery of the melting furnace 1 as shown in FIG. When the induction heating coil 18 is used, for example, the melting furnace 1 is made of a non-magnetic material such as ceramic, and the perforated separation plate 15 is made of the structural steel SS41 as described above.

【0026】また、本実施例では廃板,廃板群からなる
被溶解物6として未化成の極板,極板群を用いたが、十
分に電解液を洗浄し乾燥させた化成後の極板,極板群を
溶解させても同様の効果が得られた。
Further, in this embodiment, the unformed electrode plate or electrode plate group was used as the material to be dissolved 6 consisting of the waste plate and the waste plate group. However, the electrode after chemical conversion, which was sufficiently washed with electrolyte and dried, was used. Similar effects were obtained by melting the plates and plates.

【0027】以上の結果は、格子体Pb−Ca系の場合
であるが、溶解時の流動性がより良好なPb−Sb系の
格子体の場合でも同等な効果が得られることは言うまで
もない。
The above results are for the case of the lattice Pb-Ca system, but it goes without saying that the same effect can be obtained even for the case of the Pb-Sb system lattice having better fluidity during dissolution.

【0028】本明細書に開示した本発明の好ましい態様
を要約して示すと、下記の通りである。
A summary of the preferred embodiments of the invention disclosed herein is as follows.

【0029】(1) 溶解炉内の上部に極板又は極板群
のいずれか一方又は双方からなる被溶解物を投入する被
溶解物投入部屋が設けられ、前記溶解炉内の下部には前
記被溶解物を熱溶解して得られた溶解鉛合金を回収する
溶解鉛合金回収部屋が設けられ、前記両部屋の間は前記
被溶解物を加熱して溶解させると共に得られた溶解鉛合
金を孔から落として分離する有孔分離板で仕切られてい
ることを特徴とする鉛蓄電池の極板,極板群の溶解装
置。
(1) A melted material charging chamber for charging a melted material composed of one or both of an electrode plate and an electrode plate group is provided in an upper part of the melting furnace, and the above-mentioned lower part of the melting furnace is provided with the above-mentioned material. A molten lead alloy recovery chamber for recovering the molten lead alloy obtained by thermally melting the substance to be melted is provided, and the molten lead alloy obtained by heating and melting the substance to be melted between the two chambers is used. A melting device for a plate or a group of plates of a lead storage battery, characterized by being partitioned by a perforated separation plate that drops from the hole and separates.

【0030】(2) 前記有孔分離板の孔の大きさは、
0.7 〜3.8 mmであることを特徴とする第1項に記載の鉛
蓄電池の極板,極板群の溶解装置。
(2) The size of the holes of the perforated separation plate is
0.7-3.8 mm, The melting | dissolution apparatus of the electrode plate and electrode plate group of the lead acid battery of Claim 1 characterized by the above-mentioned.

【0031】(3) 前記溶解炉の底部は漏斗状のテー
パ形に形成され、このテーパ形の底部の末端に溶解鉛合
金回収穴が設けられていることを特徴とする第1項又は
第2項に記載の鉛蓄電池の極板,極板群の溶解装置。
(3) The bottom of the melting furnace is formed in a funnel-shaped tapered shape, and a molten lead alloy recovery hole is provided at the end of the tapered bottom, wherein Dissolution device for the electrode plate and electrode plate group of the lead storage battery according to the item.

【0032】(4) 前記溶解炉の外には前記有孔分離
板を加熱する電熱ヒータが設けられていることを特徴と
する第1項,第2項又は第3項のいずれか1つに記載の
鉛蓄電池の極板,極板群の溶解装置。
(4) An electrothermal heater for heating the perforated separation plate is provided outside the melting furnace according to any one of the first, second and third aspects. Dissolution device for the electrode plate and electrode plate group of the lead storage battery described above.

【0033】(5) 非磁性材からなる前記溶解炉の外
には前記有孔分離板を加熱する誘導加熱コイルが設けら
れていることを特徴とする第1項,第2項又は第3項の
いずれか1つに記載の鉛蓄電池の極板,極板群の溶解装
置。
(5) An induction heating coil for heating the perforated separation plate is provided outside the melting furnace made of a non-magnetic material. The lead-acid battery electrode plate or electrode plate assembly melting device described in any one of 1.

【0034】(6) 前記有孔分離板が電熱ヒータを内
蔵していることを特徴とする第1項,第2項又は第3項
のいずれか1つに記載の鉛蓄電池の極板,極板群の溶解
装置。
(6) The lead-acid battery electrode plate and electrode according to any one of the first, second and third items, wherein the perforated separation plate has a built-in electrothermal heater. Plate group melting device.

【0035】[0035]

【発明の効果】以上説明したように本発明に係る鉛蓄電
池の極板,極板群の溶解装置によれば、下記のような優
れた効果を得ることができる。
As described above, according to the melting device for the electrode plate and the electrode plate group of the lead storage battery according to the present invention, the following excellent effects can be obtained.

【0036】本発明では溶解炉内に有孔分離板を配置
し、その上に極板,極板群からなる被溶解物を載せ、該
被溶解物を有孔分離板で直接加熱するので、格子体の溶
解が速やかに起こり、酸化して活物質に付着する鉛合金
量を減少させることができる。また本発明によれば、活
物質のみが有孔分離板上に堆積し、溶解鉛合金が該有孔
分離板の孔を通り抜けて下の溶解鉛合金回収部屋に落下
するので、溶解部分と不溶解部分の分離を容易に行うこ
とができる。このため本発明によれば、鉛合金の回収率
を増加させることができ、発生する廃棄物量を削減する
ことができる。
In the present invention, since the perforated separation plate is arranged in the melting furnace, the material to be melted consisting of the electrode plate and the electrode plate group is placed thereon, and the material to be melted is directly heated by the perforated separation plate. It is possible to rapidly dissolve the lattice and oxidize it to reduce the amount of the lead alloy adhering to the active material. Further, according to the present invention, since only the active material is deposited on the perforated separation plate, and the molten lead alloy passes through the holes of the perforated separation plate and falls into the molten lead alloy recovery chamber below, the molten portion is not mixed with the molten portion. The dissolved portion can be easily separated. Therefore, according to the present invention, the recovery rate of the lead alloy can be increased and the amount of waste generated can be reduced.

【0037】また本発明では、有孔分離板の孔の大きさ
を0.7 〜3.8 mmに設定することにより、孔の大きさが3.
8 mmより大きい場合に生ずる該有孔分離板の孔から活物
質も落下して溶解鉛合金の中に混入されるのを回避で
き、また孔の大きさが0.7 mmより小さい場合に生ずる溶
解鉛合金が該孔から通り抜け難くなるのを回避でき、効
率よく溶解鉛合金の回収を行うことができる。
Further, in the present invention, the hole size of the perforated separation plate is set to 0.7 to 3.8 mm, so that the hole size becomes 3.
It is possible to prevent the active material from falling through the holes of the perforated separation plate when it is larger than 8 mm to be mixed into the molten lead alloy, and to dissolve molten lead when the size of the hole is smaller than 0.7 mm. It is possible to prevent the alloy from being difficult to pass through the holes, and it is possible to efficiently recover the molten lead alloy.

【0038】また、溶解鉛合金回収部屋の下部に溶解鉛
合金回収穴を設けることにより、溶解炉からの溶解鉛合
金の回収を容易に行うことができる。
Further, by providing the molten lead alloy recovery hole in the lower portion of the molten lead alloy recovery chamber, it is possible to easily recover the molten lead alloy from the melting furnace.

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

【図1】(A)は本発明に係る鉛蓄電池の極板,極板群
の溶解装置における一実施例を示す平面図、(B)は
(A)に示す溶解装置の溶解前のX−X線断面図、
(C)は(A)に示す溶解装置の溶解中及び回収時のX
−X線断面図である。
FIG. 1 (A) is a plan view showing an embodiment of a melting device for a plate and a plate group of a lead storage battery according to the present invention, and FIG. 1 (B) is an X- state before melting of the melting device shown in FIG. X-ray sectional view,
(C) is X during dissolution and recovery of the dissolution apparatus shown in (A)
It is a X-ray sectional view.

【図2】本発明に係る溶解装置で有孔分離板の孔の大き
さを変えた場合の鉛合金の回収率の変化を示す図であ
る。
FIG. 2 is a diagram showing changes in the recovery rate of lead alloy when the size of the holes of the perforated separation plate is changed in the melting apparatus according to the present invention.

【図3】本発明に係る溶解装置で用いる有孔分離板の他
の例を示す要部斜視図である。
FIG. 3 is a main part perspective view showing another example of a perforated separation plate used in the melting apparatus according to the present invention.

【図4】本発明に係る鉛蓄電池の極板,極板群の溶解装
置における他の実施例を示す縦断面図である。
FIG. 4 is a vertical cross-sectional view showing another embodiment of the melting device for the electrode plate and the electrode plate group of the lead storage battery according to the present invention.

【図5】(A)は従来の鉛蓄電池の極板,極板群の溶解
装置を示す平面図、(B)は(A)に示す溶解装置の溶
解前のY−Y線断面図、(C)は(A)に示す溶解装置
の溶解中のY−Y線断面図、(D)は(A)に示す溶解
装置の溶解終期のY−Y線断面図、(E)は(A)に示
す溶解装置の回収時のY−Y線断面図である。
FIG. 5A is a plan view showing a conventional electrode plate of a lead storage battery and a melting device for a plate group; FIG. 5B is a cross-sectional view of the melting device shown in FIG. (C) is a sectional view taken along line YY of the melting apparatus shown in (A), (D) is a sectional view taken along line YY at the end of melting of the melting apparatus shown in (A), and (E) is (A). FIG. 7 is a cross-sectional view taken along the line YY at the time of recovery of the melting device shown in FIG.

【符号の説明】[Explanation of symbols]

1 溶解炉 1a 扉 2 底板 3 溶解室 4 重油バーナ 5 溶解浴 6 被溶解物 7 溶解鉛合金 8 活物質及び未溶解合金 9 ポンプ 10 吸上げパイプ 11 吐出パイプ 12 回収缶 13 被溶解物投入部屋 14 溶解鉛合金回収部屋 15 有孔分離板 15a 孔 15b シーズヒータ 16 電熱ヒータ 17 溶解鉛合金回収穴 18 誘導加熱コイル 1 Melting furnace 1a Door 2 Bottom plate 3 Melting chamber 4 Heavy oil burner 5 Melting bath 6 Melting material 7 Melting lead alloy 8 Active material and unmelting alloy 9 Pump 10 Suction pipe 11 Discharge pipe 12 Recovery can 13 Melting material input room 14 Molten lead alloy recovery room 15 Perforated separation plate 15a Hole 15b Sheath heater 16 Electric heater 17 Molten lead alloy recovery hole 18 Induction heating coil

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 溶解炉内の上部に極板又は極板群のいず
れか一方又は双方からなる被溶解物を投入する被溶解物
投入部屋が設けられ、前記溶解炉内の下部には前記被溶
解物を熱溶解して得られた溶解鉛合金を回収する溶解鉛
合金回収部屋が設けられ、前記両部屋の間は前記被溶解
物を加熱して溶解させると共に得られた溶解鉛合金を孔
から落として分離する有孔分離板で仕切られていること
を特徴とする鉛蓄電池の極板,極板群の溶解装置。
1. A melted material charging chamber for charging a melted material composed of one or both of an electrode plate and a group of electrode plates is provided in an upper portion of the melting furnace, and the melted material is placed in a lower portion of the melting furnace. A molten lead alloy recovery chamber for recovering the molten lead alloy obtained by thermally melting the melted substance is provided, and the molten lead alloy obtained by heating and melting the melted substance is provided between the two chambers. Dissolving device for a lead-acid battery electrode plate or electrode plate group, characterized by being separated by a perforated separation plate that is dropped and separated.
【請求項2】 前記有孔分離板の孔の大きさは、0.7 〜
3.8 mmであることを特徴とする請求項1記載の鉛蓄電池
の極板,極板群の溶解装置。
2. The size of the holes of the perforated separation plate is from 0.7 to
3. The melting device for the electrode plate and the electrode plate group of the lead storage battery according to claim 1, which is 3.8 mm.
【請求項3】 前記溶解炉には前記溶解鉛合金回収部屋
の下部に溶解鉛合金回収穴が設けられていることを特徴
とする請求項1又は2に記載の鉛蓄電池の極板,極板群
の溶解装置。
3. The lead plate of a lead storage battery according to claim 1 or 2, wherein the melting furnace is provided with a molten lead alloy recovery hole at a lower portion of the molten lead alloy recovery chamber. Fusing device.
【請求項4】 前記溶解炉の外には前記有孔分離板を加
熱する電熱ヒータが設けられていることを特徴とする請
求項1,2又は3のいずれか1つに記載の鉛蓄電池の極
板,極板群の溶解装置。
4. The lead-acid battery according to claim 1, wherein an electric heater for heating the perforated separation plate is provided outside the melting furnace. Dissolution device for plates and plates.
【請求項5】 前記溶解炉の外には前記有孔分離板を加
熱する誘導加熱コイルが設けられていることを特徴とす
る請求項1,2又は3のいずれか1つに記載の鉛蓄電池
の極板,極板群の溶解装置。
5. The lead storage battery according to claim 1, wherein an induction heating coil for heating the perforated separation plate is provided outside the melting furnace. Dissolution device for electrode plates and electrode plates.
【請求項6】 前記有孔分離板が電熱ヒータを内蔵して
いることを特徴とする請求項1,2又は3のいずれか1
つに記載の鉛蓄電池の極板,極板群の溶解装置。
6. The perforated separation plate has a built-in electrothermal heater.
The lead-acid battery electrode plate and electrode plate assembly melting device described in 1.
JP17671394A 1994-07-28 1994-07-28 Dissolution device for electrode plates and electrode plates of lead acid batteries Withdrawn JPH0845565A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17671394A JPH0845565A (en) 1994-07-28 1994-07-28 Dissolution device for electrode plates and electrode plates of lead acid batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17671394A JPH0845565A (en) 1994-07-28 1994-07-28 Dissolution device for electrode plates and electrode plates of lead acid batteries

Publications (1)

Publication Number Publication Date
JPH0845565A true JPH0845565A (en) 1996-02-16

Family

ID=16018465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17671394A Withdrawn JPH0845565A (en) 1994-07-28 1994-07-28 Dissolution device for electrode plates and electrode plates of lead acid batteries

Country Status (1)

Country Link
JP (1) JPH0845565A (en)

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JP2008106344A (en) * 2006-09-25 2008-05-08 Furukawa Battery Co Ltd:The Method for manufacturing substrate for lead storage battery and manufacturing apparatus therefor
JP2009007622A (en) * 2007-06-27 2009-01-15 Furukawa Battery Co Ltd:The Method for melting lead scrap, and method for manufacturing substrate for lead battery and manufacturing method thereof
JP2022147471A (en) * 2021-03-23 2022-10-06 古河電気工業株式会社 Material collecting method for bipolar storage battery

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008106344A (en) * 2006-09-25 2008-05-08 Furukawa Battery Co Ltd:The Method for manufacturing substrate for lead storage battery and manufacturing apparatus therefor
JP2009007622A (en) * 2007-06-27 2009-01-15 Furukawa Battery Co Ltd:The Method for melting lead scrap, and method for manufacturing substrate for lead battery and manufacturing method thereof
JP2022147471A (en) * 2021-03-23 2022-10-06 古河電気工業株式会社 Material collecting method for bipolar storage battery

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