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JP3947452B2 - Non-ferrous metal scrap melting furnace - Google Patents

Non-ferrous metal scrap melting furnace Download PDF

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Publication number
JP3947452B2
JP3947452B2 JP2002313240A JP2002313240A JP3947452B2 JP 3947452 B2 JP3947452 B2 JP 3947452B2 JP 2002313240 A JP2002313240 A JP 2002313240A JP 2002313240 A JP2002313240 A JP 2002313240A JP 3947452 B2 JP3947452 B2 JP 3947452B2
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Japan
Prior art keywords
molten metal
vortex chamber
chamber
pump
melting furnace
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JP2002313240A
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Japanese (ja)
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JP2004149815A (en
Inventor
一雄 日下
真敏 寺西
中村  清
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Sanken Sangyo Co Ltd
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Sanken Sangyo Co Ltd
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Priority to JP2002313240A priority Critical patent/JP3947452B2/en
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  • Manufacture And Refinement Of Metals (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、アルミニウムやアルミニウム合金等の非鉄金属のうち、鋳造品を機械加工する際に発生する切粉、スラブやビレットの皮むき過程で発生するスカルピングチップ、使用済み飲料缶の破砕屑、サッシの破砕屑、その他のスクラップ小片(以下、単に屑という。)を溶解する溶解炉に関するものである。
【0002】
【従来の技術】
アルミニウムやアルミニウム合金等の非鉄金属を加工したり、スクラップをリサイクルする過程で大量の屑が発生するが、これらの屑を再利用するために溶解炉で溶融している。これらの屑は薄肉で嵩比重が小さいので、溶湯表面上へ投下すると、溶湯の表面張力と酸化膜に遮られて溶湯上に浮き、この間高温の酸化性雰囲気にさらされ、その多くは溶解せずに夥しい酸化物となる。このため、溶湯の表面下へ迅速に屑を沈めることがこれら屑溶解の効果的な必須条件とされ、溶湯に屑を巻き込むために渦流を発生させたり、乱流を発生させる等の方法及び装置が伝統的に考案されてきた。溶湯に渦流や乱流を発生させるための駆動源としては、電動モーターやエアモーターによる溶湯循環ポンプを用いるものと、磁界を移動させるいわゆる電磁力を用いるものに大別される。
このような非鉄金属屑溶解炉としては、下記に提示の特許文献1および特許文献2に開示のものがある。
【0003】
【特許文献1】
特許第2554510号公報
【特許文献2】
米国特許第6217823号明細書
【0004】
特許文献1に開示の溶解炉は、図6に示すように、昇温室2、渦室10および暗渠部11を備え、暗渠部11と昇温室2との間にポンプ3を設けている。そして、このポンプ3を稼動して溶湯Mを循環させながら、渦室10に非鉄金属の屑を投入する。投入された屑は、渦室10および暗渠部11で溶解され、溶湯Mとなって昇温室2に至る仕組みである。なお、渦室10の側壁は垂直面10aを構成している。
【0005】
また、特許文献2に開示のものは、図7に示すように、渦室20の下端部を断面逆円錐状の傾斜壁20aとし、この傾斜壁20aの下側に連通する上向流路21から溶湯Mをポンプで送り込み、当該溶湯Mを傾斜壁20aに沿って上向きに渦巻き状に流入させた後、その自重で吐出口22から流出させている。
【0006】
【発明が解決しようとする課題】
屑を迅速に溶湯表面下へ沈めることは必須条件であるが、屑は完全に溶解し終えるまである程度時間を要するので、浮きやすい屑を引き続き溶湯表面下へ滞留させておくことがさらに必要である。
特許文献1に開示された溶解炉は、渦室10の底部に径の狭い吐出口10bを設けているので、ポンプ3を稼動すると溶湯は昇温室2から渦室10へ誘導されて渦室10で層流の渦を形成して屑を迅速に巻き込み、さらに吐出口10bを通過することによって流速を与えられた溶湯が引き続いて屑を滞留させたまま暗渠部11及びポンプ3を通過する間に、屑は完全に溶解し、再び昇温室2へ戻る。巻き込んだ屑が直ちに溶湯表面上へ浮上することがないので酸化ロスの少ない優れた溶解炉である。
【0007】
しかしながら、図6に示す溶解炉では、渦室10に投下した屑に紛れた鉄片等の異物がポンプ3に達したり、厚肉の屑が完全に溶解し終えないうちにポンプ3に達し、ポンプ3が損傷するという問題が間々あった。
また、暗渠部11にはドロスが堆積し、定期的に清掃しなければならないという問題もあった。
【0008】
また、図7に示したような溶解炉は、傾斜壁20aに沿って上向きの渦巻き状に溶湯を流入させながら渦室20へ溶湯Mを導入し、その後溶湯Mの自重によって吐出口22から流出させている。このため、溶湯Mは渦室20において強大な渦を形成し得ず、また自重によって吐出口22を通過するだけの溶湯には屑を引き続き溶湯表面下へ滞留させるだけの十分な流速が与えられず、屑は吐出口22の下流側で溶湯表面上に浮きやすいという問題がある。その結果、浮上した屑は高温の酸化性雰囲気にさらされて酸化ロスとなる。
【0009】
そこで、本発明の目的とするところは、屑をポンプに達するまでに完全に溶解させて、ポンプの損傷を未然に防止することができ、かつ、酸化ロスの少ない優れた非鉄金属屑の溶解炉を提供することにある。
また他の目的は、ポンプにかえて電磁誘導装置を使用した場合であっても、屑を完全に溶解させて、酸化ロスの少ない優れた非鉄金属屑の溶解炉を提供することにある。
【0010】
【課題を解決するための手段】
上記の目的を達成するために、本発明の請求項1に記載の非鉄金属屑溶解炉は、溶湯(M)を加温するバーナー(6)を備えた昇温室(2)と、非鉄金属の屑が投入される渦室(1)と、溶湯(M)を循環させるポンプ(3)とを備えた溶解炉において、前記渦室(1)を前記ポンプ(3)の下流側直近で、かつ、前記昇温室(2)の上流側で、しかも、前記渦室(1)の下部に設けられた吐出口(1c)を前記昇温室(2)の湯面(S)より低い位置で溶湯(M)内に設けるとともに、前記渦室(1)の下部を、テーパー壁(1a)によって略逆円錐状とし、その上、前記ポンプ(3)の吐出口から前記渦室(1)に至るまでの流路(5)の底面を前記渦室(1)側に向かって傾斜した上昇面(5a)とし、前記ポンプ(3)の吐出力で、前記溶湯(M)を、前記ポンプ(3)の吐出口(1c)から前記上昇面(5a)を通して前記昇温室(2)の湯面(S)より高いレベルから渦室(1)へ渦巻き状に供給し、その渦室(1)から前記昇温室(2)の湯面(S)より低い位置に供給してなることを特徴とする。
【0012】
また、請求項2に記載の非鉄金属屑溶解炉は、前記請求項1に記載の発明において、前記溶湯(M)を、螺旋状の案内路(4)を介して、テーパー壁(1a)の上端部へ供給してなることを特徴とする。
【0014】
なお、括弧内の記号は、図面および後述する発明の実施の形態に記載された対応要素または対応事項を示す。
【0015】
本発明の請求項1に記載の非鉄金属屑溶解炉によれば、ポンプの吐出力で、溶湯を昇温室の湯面より高いレベルから、高所から低所へ流下させるように渦室へ渦巻き状に供給するので、層流の強大な渦を形成することができ、これによって屑を迅速かつ効果的に溶湯中へ巻き込むことができる。
さらに、屑を巻き込んだ溶湯は、ポンプの吐出力によって、渦室下部の吐出口を通過する際に流速が与えられ、溶湯は巻き込んだ屑を滞留させたまま渦室の下流側へ吐出される。
【0016】
さらに渦室をポンプの下流側直近で、かつ、昇温室の上流側に設けているので、渦室に投下された屑を、当該渦室およびその下流側に位置する昇温室において完全に溶解させることができる。
従って、非溶解状態の屑がポンプに達することがなく、また仮に屑に鉄片等の異物が紛れていたとしても、これらはポンプの下流側の昇温室で沈降するので、これにより、ポンプの損傷を未然に防止することができる。
【0017】
またさらに、渦室へ投下した屑を、ポンプに達するまでに完全に溶解させることができるので、従来のような暗渠部を必要としない。従って、溶解炉の小型化と暗渠部の定期的な清掃が省略できる利便性を与える。
【0021】
また、請求項1に記載の発明によれば、渦室の下部を、断面略逆円錐状のテーパー壁としているので、渦室にテーパー壁を形成してない図6に示した溶解炉と異なり、強大な渦巻き流を容易に形成することができる。
このテーパー壁はまた、形成された溶湯の渦巻き流が渦室から吐出される際に、ポンプの吐出力又は電磁誘導装置の電磁力とあいまって、溶湯に流速を与える。
これにより、投下された屑をより迅速に溶解することができ、屑の酸化ロスを低減するとともに、ポンプを使用した場合、ポンプの損傷をさらに確実に防止することができる。
【0022】
さらに、請求項2に記載の発明によれば、溶湯を、案内路を介して、テーパー壁の上端部へ供給するので、当該テーパー壁によって、強大な渦巻き流を円滑に形成することができる。従って、屑を迅速に溶湯に巻き込み、酸化ロスをさらに低減することができる。
【0023】
【発明の実施の形態】
図1乃至図4を参照して、本発明の実施形態に係る非鉄金属屑溶解炉について説明する。図1は本発明の実施形態に係る非鉄金属屑溶解炉を示す概略斜視図であり、図2はその非鉄金属屑溶解炉の要部を示す縦断面図である。また、図3は図1における溶解炉の渦室1を示す平面図であり、図4はそのA−A線断面図である。なお、従来例で示したものと同一部分には同一符号を付した。
【0024】
本発明の実施形態に係る非鉄金属屑溶解炉は、アルミニウム又はアルミニウム合金の屑を溶解するものであり、昇温室2と渦室1とそしてポンプ3とを備えるものである。
昇温室2には、複数のバーナー6が設けられ、このバーナー6によって溶湯Mを加温する。渦室1には屑が投入される。また、ポンプ3は、溶解炉内の溶湯Mを循環させる。
【0025】
こうした構成において、渦室1を、ポンプ3の下流側直近で、かつ、昇温室2の上流側に設け、当該ポンプ3の吐出力で、溶湯Mを昇温室2の湯面Sより高いレベルから渦室1へ渦巻き状に供給する。同時に、ポンプ3から渦室1に至るまでの流路5の底面を上昇面5aとし、渦室1に流入する溶湯Mの湯面Sが、より容易に昇温室2の湯面Sより高いレベルに達するように設定している。
【0026】
また、渦室1を、その上部を垂直壁1bで構成した円筒状とすると共に、その下部をテーパー壁1aによって略逆円錐状とし、さらに、溶湯Mを、螺旋状の案内路4を介して、テーパー壁1aの上端部へ供給するようにしている。
【0027】
この非鉄金属屑溶解炉において、ポンプ3を稼動すると溶湯Mが昇温室2の湯面Sより高いレベルから渦室1のテーパー壁1a上端部へ供給される。供給された溶湯Mは、テーパー壁1aに沿い吐出口1cへ向かって流下するため大きな渦巻き流を形成する。従って、この渦室1へ投下された屑は、渦巻き流によって迅速かつ効果的に溶解する。
【0028】
ポンプ3の吐出力によって流速を与えられながら渦室1の吐出口1cから吐き出された溶湯Mは屑を溶湯Mに滞留させたまま昇温室2へ達し、この昇温室2に設置されたバーナー6によって加温され、上記滞留中に未だ溶解し終えなかった屑があったとしてもこの昇温室2で完全に溶解される。
【0029】
昇温室2で加温された溶湯Mは、ポンプ3の吸引力によって再び渦室1へ供給される。このとき、先に渦室1へ投入された屑は完全に溶解しているため、未溶解状態のままポンプ3に達することがない。
また、屑に紛れた鉄片等の異物は渦室1を通過し、溶湯Mの流速で昇温室2に運ばれて沈降し、ポンプ3には達しない。これらの沈降した異物は適宜行われる溶湯Mの浄化乃至除滓作業中に昇温室2から除去できる。
従って、渦室1へ投下した屑によってポンプ3を損傷させることがない。
【0030】
また、この溶解炉においては、渦室1へ投下した屑を、ポンプ3に達するまでに完全に溶解させることができるので、暗渠部を必要としない。従って、溶解炉の小型化を図ることができるとともに暗渠部の定期的清掃もなくせる。
【0031】
なお、図5に示すように、ポンプ3にかえて電磁誘導装置30を設け、その電磁誘導装置30の磁界を移動させる電磁力によって、溶湯Mを昇温室2の湯面Sより高いレベルから渦室1へ渦巻き状に供給するように溶湯Mを循環させることもできる。
この場合、渦室1を電磁誘導装置30の下流側直近で、かつ、昇温室2の上流側に設けるようにする。
【0032】
これによれば、電磁誘導装置30の磁界を移動させる電磁力によって、溶湯Mを昇温室2の湯面Sより高いレベルから、高所から低所へ流下させるように渦室1へ渦巻き状に供給するので、層流の強大な渦を形成することができ、これによって屑を迅速かつ効果的に溶湯中へ巻き込むことができる。
さらに、屑を巻き込んだ溶湯Mは、電磁誘導装置30の磁界を移動させる電磁力によって、渦室1下部の吐出口1cを通過する際に流速が与えられ、溶湯Mは巻き込んだ屑を滞留させたまま渦室1の下流側へ吐出される。
【0033】
さらに渦室1を電磁誘導装置30の下流側直近で、かつ、昇温室2の上流側に設けているので、渦室1に投下された屑を、当該渦室1およびその下流側に位置する昇温室2において完全に溶解させることができる。
【0034】
またさらに、渦室1へ投下した屑を、電磁誘導装置30に達するまでに完全に溶解させることができるので、暗渠部を必要としない。従って、溶解炉の小型化と暗渠部の定期的な清掃が省略できる利便性を与える。
【0035】
【発明の効果】
以上のとおり、本発明の請求項1に記載の非鉄金属屑溶解炉によれば、渦室をポンプの下流側直近で、かつ、昇温室の上流側に設けているので、渦室に投下された屑は当該渦室およびその下流側に位置する昇温室において完全に溶解させることができる。また屑に紛れた鉄片等の異物は渦室を通過し、溶湯の流速で昇温室に運ばれて沈降する。沈降した異物は適宜行われる溶湯の浄化乃至除滓作業中に容易に除去できる。従って、未溶解の屑も鉄片等の異物もポンプに達することがなく、これにより、ポンプの損傷を未然に防止することができる。
【0036】
また、ポンプの吐出力で、溶湯を昇温室の湯面より高いレベルから、高所から低所へ流下させるように渦室へ渦巻き状に供給するので、強大な渦巻き流を形成することができ、これによっても屑を迅速かつ効果的に溶解することができ、ポンプの損傷を防止することができる。
【0037】
さらに、渦室へ投下した屑を、ポンプに達するまでに完全に溶解させることができるので、従来のような暗渠部を必要としない。従って、溶解炉の小型化を図ることができるとともに暗渠部の定期的清掃もなくせる。。
【0041】
また、請求項1に記載の発明によれば、渦室の下部を、断面略逆円錐状のテーパー壁としているので、さらに強大な渦巻き流を形成することができる。これにより、投下された屑をより迅速に溶解することができ、ポンプを使用した場合、ポンプの損傷をさらに確実に防止することができる共に、経済性のさらなる向上を図ることができる。
【0042】
さらに、請求項2に記載の発明によれば、溶湯を、案内路を介して、テーパー壁の上端部へ供給するので、当該テーパー壁によって、強大な渦巻き流を円滑に形成することができ、これにより、ポンプを使用した場合、ポンプの損傷をより未然に防止するとともに屑の酸化ロスを低減し、経済性をさらに向上させることができる。
【図面の簡単な説明】
【図1】本発明の実施形態に係る非鉄金属屑溶解炉を示す概略斜視図である。
【図2】本発明の実施形態に係る非鉄金属屑溶解炉の要部を示す縦断面図である。
【図3】図1における溶解炉の渦室を示す平面図である。
【図4】図3のA−A線断面図である。
【図5】本発明の実施形態に係る他の非鉄金属屑溶解炉の要部を示す縦断面図である。
【図6】従来例に係る非鉄金属屑溶解炉の要部を示す縦断面図である。
【図7】他の従来例に係る非鉄金属屑溶解炉の渦室を示す縦断面図である。
【符号の説明】
1 渦室
1a テーパー壁
1b 垂直壁
1c 吐出口
2 昇温室
3 ポンプ
4 案内路
5 流路
5a 上昇面
6 バーナー
10 渦室
10a 垂直面
11 暗渠部
11b 吐出口
20 渦室
20a 傾斜壁
21 上向流路
22 吐出口
M 溶湯
S 湯面
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to non-ferrous metals such as aluminum and aluminum alloys, chips generated during machining of cast products, sculpting chips generated during the peeling process of slabs and billets, crushed waste from used beverage cans, sashes The present invention relates to a melting furnace for melting crushed scraps and other scrap pieces (hereinafter simply referred to as scraps).
[0002]
[Prior art]
A large amount of waste is generated in the process of processing non-ferrous metals such as aluminum and aluminum alloys and recycling scrap, but these wastes are melted in a melting furnace to be reused. Since these scraps are thin and have a low bulk specific gravity, when dropped on the surface of the molten metal, they float on the molten metal due to the surface tension of the molten metal and the oxide film, and during this time they are exposed to a high-temperature oxidizing atmosphere. It becomes a ugly oxide. For this reason, it is considered as an effective essential condition for melting these scraps to quickly sink the waste below the surface of the molten metal, and a method and an apparatus for generating vortex or turbulent flow to entrain the molten metal in the molten metal. Has been traditionally devised. Driving sources for generating vortex and turbulent flow in the molten metal are roughly classified into those using a molten metal circulation pump using an electric motor or an air motor and those using a so-called electromagnetic force that moves a magnetic field.
Such non-ferrous metal scrap melting furnaces are disclosed in Patent Document 1 and Patent Document 2 presented below.
[0003]
[Patent Document 1]
Japanese Patent No. 2554510 [Patent Document 2]
US Pat. No. 6,217,823 Specification
As shown in FIG. 6, the melting furnace disclosed in Patent Document 1 includes a heating chamber 2, a vortex chamber 10, and a culvert portion 11, and a pump 3 is provided between the culvert portion 11 and the heating chamber 2. And while operating this pump 3 and circulating the molten metal M, scraps of non-ferrous metal are put into the vortex chamber 10. The thrown-in waste is melted in the vortex chamber 10 and the culvert portion 11, and becomes a molten metal M that reaches the temperature raising chamber 2. The side wall of the vortex chamber 10 constitutes a vertical surface 10a.
[0005]
Further, as disclosed in Patent Document 2, as shown in FIG. 7, the lower end portion of the vortex chamber 20 is an inclined wall 20a having an inverted conical cross section, and an upward flow channel 21 communicating with the lower side of the inclined wall 20a. Then, the molten metal M is pumped in, and the molten metal M is swirled upward along the inclined wall 20a, and then flows out of the discharge port 22 by its own weight.
[0006]
[Problems to be solved by the invention]
It is an essential condition to quickly submerge the debris below the surface of the melt, but it takes a certain amount of time for the debris to completely dissolve, so it is further necessary to continue to retain debris that tends to float below the surface of the melt. .
Since the melting furnace disclosed in Patent Document 1 is provided with a discharge port 10b having a narrow diameter at the bottom of the vortex chamber 10, the molten metal is guided from the temperature raising chamber 2 to the vortex chamber 10 when the pump 3 is operated. During the passage of the molten metal given the flow velocity by passing through the discharge port 10b and passing through the culvert portion 11 and the pump 3 while retaining the waste, the laminar flow vortex is formed and the waste is rapidly wound. The waste is completely dissolved and returned to the heating chamber 2 again. It is an excellent melting furnace with little oxidation loss because the entrained scrap does not immediately float on the surface of the molten metal.
[0007]
However, in the melting furnace shown in FIG. 6, foreign matter such as iron pieces mixed in the scrap dropped in the vortex chamber 10 reaches the pump 3 or reaches the pump 3 before the thick scrap is completely melted. There was a problem that 3 was damaged.
In addition, there is a problem that dross accumulates in the underdrain portion 11 and must be periodically cleaned.
[0008]
In addition, the melting furnace as shown in FIG. 7 introduces the molten metal M into the vortex chamber 20 while flowing the molten metal in an upward spiral along the inclined wall 20a, and then flows out from the discharge port 22 due to its own weight. I am letting. For this reason, the molten metal M cannot form a strong vortex in the vortex chamber 20, and the molten metal that simply passes through the discharge port 22 by its own weight is given a flow velocity sufficient to keep the debris below the molten metal surface. In other words, there is a problem that the waste tends to float on the molten metal surface on the downstream side of the discharge port 22. As a result, the surfacing waste is exposed to a high-temperature oxidizing atmosphere, resulting in oxidation loss.
[0009]
Therefore, the object of the present invention is to completely dissolve the scrap before reaching the pump, to prevent the pump from being damaged, and to have an excellent nonferrous metal scrap melting furnace with little oxidation loss. Is to provide.
Another object of the present invention is to provide an excellent nonferrous metal scrap melting furnace with little oxidation loss by completely melting scrap even when an electromagnetic induction device is used instead of a pump.
[0010]
[Means for Solving the Problems]
In order to achieve the above object, a nonferrous metal scrap melting furnace according to claim 1 of the present invention includes a heating chamber (2) provided with a burner (6) for heating the molten metal (M), a nonferrous metal In a melting furnace provided with a vortex chamber (1) into which scraps are charged and a pump (3) for circulating molten metal (M), the vortex chamber (1) is located immediately downstream of the pump (3), and The discharge port (1c) provided on the upstream side of the temperature raising chamber (2) and at the lower part of the vortex chamber (1) is positioned at a position lower than the hot water surface (S) of the temperature raising chamber (2). M) and the lower part of the vortex chamber (1) is formed into a substantially inverted conical shape by a tapered wall (1a), and further from the discharge port of the pump (3) to the vortex chamber (1). in the flow path (5) the bottom of the vortex chamber (1) elevated surface inclined toward the side and (5a), the discharge force of the pump (3), The molten metal (M) is swirled from the discharge port (1c) of the pump (3) through the rising surface (5a) to a swirl chamber (1) from a level higher than the hot water surface (S) of the heating chamber (2). The vortex chamber (1) is supplied to a position lower than the hot water surface (S) of the temperature raising chamber (2).
[0012]
A non-ferrous metal scrap melting furnace according to claim 2 is the invention according to claim 1 , wherein the molten metal (M) is passed through the spiral guide path (4) to the tapered wall (1a). It supplies to an upper end part, It is characterized by the above-mentioned.
[0014]
Symbols in parentheses indicate corresponding elements or corresponding matters described in the drawings and embodiments of the invention described later.
[0015]
According to the nonferrous metal scrap melting furnace of claim 1 of the present invention, the vortex is swirled into the vortex chamber so that the molten metal flows down from a level higher than the hot water surface of the heating chamber from a high place to a low place by the discharge force of the pump. Therefore, it is possible to form a strong laminar vortex, whereby the waste can be quickly and effectively wound into the molten metal.
Further, the molten metal entrained with debris is given a flow velocity when passing through the discharge port at the lower part of the vortex chamber by the discharge force of the pump, and the molten metal is discharged downstream of the vortex chamber while retaining the entrained debris. .
[0016]
Furthermore, since the vortex chamber is provided immediately downstream of the pump and upstream of the heating chamber, the waste dropped in the vortex chamber is completely dissolved in the vortex chamber and the heating chamber located downstream of the vortex chamber. be able to.
Therefore, non-dissolved waste does not reach the pump, and even if foreign matter such as iron pieces is mixed into the waste, they settle in the heating chamber downstream of the pump, which causes damage to the pump. Can be prevented in advance.
[0017]
Furthermore, since the waste thrown into the vortex chamber can be completely dissolved by the time it reaches the pump, a conventional culvert portion is not required. Therefore, the convenience that the downsizing of the melting furnace and the periodic cleaning of the culvert can be omitted is provided.
[0021]
Further, according to the invention described in claim 1 , since the lower part of the vortex chamber is a tapered wall having a substantially inverted conical section, unlike the melting furnace shown in FIG. 6 in which the tapered wall is not formed in the vortex chamber. A powerful spiral flow can be easily formed.
The tapered wall also gives a flow rate to the molten metal when combined with the discharge force of the pump or the electromagnetic force of the electromagnetic induction device when the swirl flow of the formed molten metal is discharged from the vortex chamber.
Thereby, the thrown-down waste can be dissolved more quickly, the oxidation loss of the waste can be reduced, and when the pump is used, damage to the pump can be prevented more reliably.
[0022]
Furthermore, according to the second aspect of the present invention, since the molten metal is supplied to the upper end portion of the tapered wall via the guide path, a strong spiral flow can be smoothly formed by the tapered wall. Therefore, scraps can be quickly caught in the molten metal, and oxidation loss can be further reduced.
[0023]
DETAILED DESCRIPTION OF THE INVENTION
With reference to FIG. 1 thru | or FIG. 4, the nonferrous metal waste melting furnace which concerns on embodiment of this invention is demonstrated. FIG. 1 is a schematic perspective view showing a non-ferrous metal scrap melting furnace according to an embodiment of the present invention, and FIG. 2 is a longitudinal sectional view showing a main part of the non-ferrous metal scrap melting furnace. 3 is a plan view showing the vortex chamber 1 of the melting furnace in FIG. 1, and FIG. 4 is a cross-sectional view taken along the line AA in FIG. In addition, the same code | symbol was attached | subjected to the same part as what was shown in the prior art example.
[0024]
A nonferrous metal scrap melting furnace according to an embodiment of the present invention melts scraps of aluminum or aluminum alloy, and includes a temperature raising chamber 2, a vortex chamber 1, and a pump 3.
The heating chamber 2 is provided with a plurality of burners 6, and the molten metal M is heated by the burners 6. Waste is introduced into the vortex chamber 1. The pump 3 circulates the molten metal M in the melting furnace.
[0025]
In such a configuration, the vortex chamber 1 is provided in the immediate vicinity of the downstream side of the pump 3 and upstream of the temperature raising chamber 2, and the molten metal M is discharged from a level higher than the level S of the temperature rising chamber 2 by the discharge force of the pump 3. The vortex chamber 1 is supplied in a spiral shape. At the same time, the bottom surface of the flow path 5 from the pump 3 to the vortex chamber 1 is the rising surface 5 a, and the level S of the molten metal M flowing into the vortex chamber 1 is more easily higher than the level S of the heating chamber 2. Is set to reach.
[0026]
In addition, the vortex chamber 1 has a cylindrical shape with an upper portion constituted by a vertical wall 1 b, and a lower portion thereof has a substantially inverted conical shape by a tapered wall 1 a, and the molten metal M is passed through a spiral guide path 4. The taper is supplied to the upper end of the taper wall 1a.
[0027]
In this non-ferrous metal scrap melting furnace, when the pump 3 is operated, the molten metal M is supplied to the upper end of the tapered wall 1a of the vortex chamber 1 from a level higher than the hot water surface S of the heating chamber 2. Since the supplied molten metal M flows down toward the discharge port 1c along the tapered wall 1a, a large spiral flow is formed. Accordingly, the waste dropped into the vortex chamber 1 is quickly and effectively dissolved by the vortex flow.
[0028]
The molten metal M discharged from the discharge port 1c of the vortex chamber 1 while being given a flow velocity by the discharge force of the pump 3 reaches the heating chamber 2 while retaining the waste in the molten metal M, and the burner 6 installed in the heating chamber 2 Even if there is debris that has not been completely dissolved during the stay, it is completely dissolved in the heating chamber 2.
[0029]
The molten metal M heated in the temperature raising chamber 2 is supplied again to the vortex chamber 1 by the suction force of the pump 3. At this time, since the waste previously thrown into the vortex chamber 1 is completely dissolved, it does not reach the pump 3 in an undissolved state.
In addition, foreign matters such as iron pieces mixed in scrap pass through the vortex chamber 1, are carried to the temperature raising chamber 2 at the flow rate of the molten metal M, and settle down, and do not reach the pump 3. These settled foreign matters can be removed from the temperature raising chamber 2 during the purification or removal work of the molten metal M performed as appropriate.
Therefore, the pump 3 is not damaged by the waste dropped into the vortex chamber 1.
[0030]
Moreover, in this melting furnace, since the waste thrown into the vortex chamber 1 can be completely dissolved before reaching the pump 3, a culvert portion is not required. Therefore, it is possible to reduce the size of the melting furnace and eliminate regular cleaning of the culvert.
[0031]
As shown in FIG. 5, an electromagnetic induction device 30 is provided instead of the pump 3, and the molten metal M is vortexed from a level higher than the hot water surface S of the heating chamber 2 by an electromagnetic force that moves the magnetic field of the electromagnetic induction device 30. The molten metal M can also be circulated so as to be spirally supplied to the chamber 1.
In this case, the vortex chamber 1 is provided immediately downstream of the electromagnetic induction device 30 and upstream of the temperature raising chamber 2.
[0032]
According to this, by the electromagnetic force that moves the magnetic field of the electromagnetic induction device 30, the molten metal M spirals into the vortex chamber 1 so as to flow down from a level higher than the hot water surface S of the heating chamber 2 from a high place to a low place. As a result of the supply, a strong laminar vortex can be formed, whereby the waste can be quickly and effectively entrained in the melt.
Further, the molten metal M in which the waste is entrained is given a flow velocity when passing through the discharge port 1c in the lower part of the vortex chamber 1 by the electromagnetic force that moves the magnetic field of the electromagnetic induction device 30, and the molten metal M retains the entrained waste. As it is, it is discharged downstream of the vortex chamber 1.
[0033]
Furthermore, since the vortex chamber 1 is provided in the immediate vicinity of the downstream side of the electromagnetic induction device 30 and on the upstream side of the temperature raising chamber 2, the waste dropped in the vortex chamber 1 is located in the vortex chamber 1 and the downstream side thereof. It can be completely dissolved in the temperature raising chamber 2.
[0034]
Furthermore, since the waste thrown into the vortex chamber 1 can be completely dissolved before reaching the electromagnetic induction device 30, a culvert portion is not required. Therefore, the convenience that the downsizing of the melting furnace and the periodic cleaning of the culvert can be omitted is provided.
[0035]
【The invention's effect】
As described above, according to the non-ferrous metal scrap melting furnace according to claim 1 of the present invention, the vortex chamber is provided in the immediate vicinity of the downstream side of the pump and the upstream side of the temperature raising chamber. The chips can be completely dissolved in the vortex chamber and the temperature raising chamber located downstream thereof. Moreover, foreign matters such as iron pieces mixed in the scraps pass through the vortex chamber, and are carried to the heating chamber at the flow rate of the molten metal and settle. The settled foreign matter can be easily removed during the purification or demolition work of the molten metal appropriately performed. Therefore, undissolved scraps and foreign matter such as iron pieces do not reach the pump, thereby preventing damage to the pump.
[0036]
In addition, the pump's discharge force causes the molten metal to be spirally supplied to the vortex chamber from a level higher than the hot water surface of the temperature raising chamber to flow from a high place to a low place, so that a strong swirl flow can be formed. This also makes it possible to dissolve the waste quickly and effectively, and to prevent damage to the pump.
[0037]
Furthermore, since the waste thrown into the vortex chamber can be completely dissolved before reaching the pump, a conventional culvert portion is not required. Therefore, it is possible to reduce the size of the melting furnace and eliminate regular cleaning of the culvert. .
[0041]
According to the first aspect of the present invention, since the lower part of the vortex chamber is a tapered wall having a substantially inverted conical section, a stronger spiral flow can be formed. Thereby, the thrown-down waste can be dissolved more quickly, and when the pump is used, damage to the pump can be prevented more reliably and economic efficiency can be further improved.
[0042]
Furthermore, according to the invention described in claim 2 , since the molten metal is supplied to the upper end portion of the tapered wall through the guide path, a strong spiral flow can be smoothly formed by the tapered wall, Thereby, when a pump is used, damage to the pump can be prevented in advance, and waste oxidation loss can be reduced, thereby further improving economic efficiency.
[Brief description of the drawings]
FIG. 1 is a schematic perspective view showing a non-ferrous metal scrap melting furnace according to an embodiment of the present invention.
FIG. 2 is a longitudinal sectional view showing a main part of the nonferrous metal scrap melting furnace according to the embodiment of the present invention.
FIG. 3 is a plan view showing a vortex chamber of the melting furnace in FIG. 1;
4 is a cross-sectional view taken along line AA in FIG.
FIG. 5 is a longitudinal sectional view showing a main part of another nonferrous metal scrap melting furnace according to an embodiment of the present invention.
FIG. 6 is a longitudinal sectional view showing a main part of a nonferrous metal scrap melting furnace according to a conventional example.
FIG. 7 is a longitudinal sectional view showing a vortex chamber of a nonferrous metal scrap melting furnace according to another conventional example.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Vortex chamber 1a Tapered wall 1b Vertical wall 1c Discharge port 2 Temperature rising chamber 3 Pump 4 Guide path 5 Flow path 5a Ascending surface 6 Burner 10 Vortex chamber 10a Vertical surface 11 Dark gutter part 11b Discharge port 20 Vortex chamber 20a Inclined wall 21 Upward flow Channel 22 Discharge port M Molten metal S Surface

Claims (2)

溶湯を加温するバーナーを備えた昇温室と、非鉄金属の屑が投入される渦室と、溶湯を循環させるポンプとを備えた溶解炉において、
前記渦室を前記ポンプの下流側直近で、かつ、前記昇温室の上流側で、しかも、前記渦室の下部に設けられた吐出口を前記昇温室の湯面より低い位置で溶湯内に設けるとともに、前記渦室の下部を、テーパー壁によって略逆円錐状とし、その上、前記ポンプの吐出口から前記渦室に至るまでの流路の底面を前記渦室側に向かって傾斜した上昇面とし、前記ポンプの吐出力で、前記溶湯を、前記ポンプの吐出口から前記上昇面を通して前記昇温室の湯面より高いレベルから渦室へ渦巻き状に供給し、その渦室から前記昇温室の湯面より低い位置に供給してなることを特徴とする非鉄金属屑溶解炉。
In a melting furnace equipped with a heating chamber equipped with a burner for heating the molten metal, a vortex chamber into which non-ferrous metal scraps are charged, and a pump for circulating the molten metal,
The vortex chamber is provided near the downstream side of the pump and upstream of the temperature raising chamber, and a discharge port provided in the lower part of the vortex chamber is provided in the molten metal at a position lower than the surface of the temperature rising chamber. In addition, the lower part of the vortex chamber has a substantially inverted conical shape by a tapered wall, and the rising surface in which the bottom surface of the flow path from the discharge port of the pump to the vortex chamber is inclined toward the vortex chamber side With the discharge force of the pump, the molten metal is spirally supplied from the pump outlet through the rising surface to a vortex chamber from a level higher than the hot water surface of the heating chamber, and from the vortex chamber to the heating chamber A non-ferrous metal scrap melting furnace characterized by being supplied to a position lower than the molten metal surface.
前記溶湯を、螺旋状の案内路を介して、前記テーパー壁の上端部へ供給してなることを特徴とする請求項1に記載の非鉄金属屑溶解炉。The non-ferrous metal scrap melting furnace according to claim 1 , wherein the molten metal is supplied to an upper end portion of the tapered wall through a spiral guide path.
JP2002313240A 2002-10-28 2002-10-28 Non-ferrous metal scrap melting furnace Expired - Lifetime JP3947452B2 (en)

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