JPH0820181B2 - Circulating non-ferrous metal scrap melting furnace - Google Patents

Circulating non-ferrous metal scrap melting furnace

Info

Publication number
JPH0820181B2
JPH0820181B2 JP4631492A JP4631492A JPH0820181B2 JP H0820181 B2 JPH0820181 B2 JP H0820181B2 JP 4631492 A JP4631492 A JP 4631492A JP 4631492 A JP4631492 A JP 4631492A JP H0820181 B2 JPH0820181 B2 JP H0820181B2
Authority
JP
Japan
Prior art keywords
molten metal
radius
impeller
line
radius vector
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.)
Expired - Lifetime
Application number
JP4631492A
Other languages
Japanese (ja)
Other versions
JPH05214457A (en
Inventor
勝己 間
一雄 日下
昇 田尻
時良 奥田
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.)
Sanken Sangyo Co Ltd
Aisin Corp
Original Assignee
Aisin Seiki Co Ltd
Sanken Sangyo 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 Aisin Seiki Co Ltd, Sanken Sangyo Co Ltd filed Critical Aisin Seiki Co Ltd
Priority to JP4631492A priority Critical patent/JPH0820181B2/en
Publication of JPH05214457A publication Critical patent/JPH05214457A/en
Publication of JPH0820181B2 publication Critical patent/JPH0820181B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、機械加工で発生するア
ルミ等の非鉄金属の金属屑やアルミ空缶等の非鉄金属屑
を迅速に溶解し、歩留まりよく再生するところの構造簡
単で保守負担の少ない非鉄金属屑溶解炉に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention quickly dissolves non-ferrous metal scraps such as aluminum and non-ferrous metal scraps such as aluminum empty cans generated by machining and recycles them with good yield. The present invention relates to a non-ferrous metal scrap melting furnace with a small amount.

【0002】[0002]

【従来の技術】従来、機械加工で発生するアルミ等の非
鉄金属の金属屑やアルミ空缶等から歩留まりよく再生す
るために、金属屑を迅速に酸化を防ぎながら溶解する溶
解炉として、底に孔を開けた円筒状容器内に金属屑を供
給し精密な溶湯ポンプ・電磁ポンプ等のポンプで溶湯を
上から注ぎ巻込み渦を作り金属屑を巻込み溶解するも
の、上下に開口端を備えた直立円筒状渦室内にその下部
に設けた複雑なインペラーで溶湯の渦を作り金属屑を巻
込むようにしたもの、その他機械的に金属屑を溶湯に浸
漬させるものが存在する。
2. Description of the Related Art Conventionally, in order to recover metal scraps of non-ferrous metals such as aluminum generated by machining from aluminum scraps and aluminum empty cans with a good yield, as a melting furnace that quickly melts metal scraps while preventing oxidation, It supplies metal scraps into a cylindrical container with holes and pours the melt from the top with a pump such as a precision melt pump or electromagnetic pump to create a vortex and melt the metal scraps. It has upper and lower open ends. There is a vertical cylindrical vortex chamber in which a molten metal vortex is formed by a complicated impeller provided in the lower part of the chamber to entrain metal scraps, and other mechanically dipping metal scraps in the melt.

【0003】しかしながら、上記従来の装置のうち、ポ
ンプを備えたものは溶湯が酸化され易く歩留まりが低く
熱効率が低くかったり、インペラーを備えたものは構造
が複雑で金属屑と接するインペラーの損傷が大きい等保
守面の負担が大きかったりすると言う問題がある。
However, among the above-mentioned conventional devices, those equipped with a pump have a low yield and low thermal efficiency because the molten metal is easily oxidized, and those equipped with an impeller have a complicated structure and damage to the impeller in contact with metal scraps. There is a problem that the maintenance load is large, such as being large.

【0004】[0004]

【発明が解決しようとする課題】解決しようとする問題
点は、上記従来のものは性能面・保守面に難があること
である。
The problem to be solved is that the above-mentioned conventional ones have problems in performance and maintenance.

【0005】[0005]

【課題を解決するための手段】本発明は、バーナー31
を備えた溶湯加熱室30の高温溶湯9dを取出して上開
渦流室20を通過させ、該渦流室20において金属屑1
0を溶かして温度の下がった低温溶湯9eを再び溶湯加
熱室30に導いて昇温する如く構成した循環型非鉄金属
溶解炉において、底42を水平面に形成したポンプハウ
ジング40の内壁41を極座標でみたとき動径Rxが極
Qの周わりを回動すると共にインペラーの半径Raより
僅かに長い最小動径Rbを始点Pbとし、極Qから徐々
に遠ざかる点が画く渦線で形成し、且つ最大同径Rdの
渦線の終点Pdから延びる接線Sdと、該接線Sdに対
し前記始点Pbから徐々に間隔を広げる線Sbとで以っ
て吐出口43の垂直両側壁44,45を構成し、前記極
Qを通る鉛直中心線を中心とし且つ前記最小動径Rbと
同一半径の円孔51を有する水平中間壁52をポンプハ
ウジング40上に形成し、前記渦線の最小動径Rbより
大きく且つ最大動径Rdより小さい半径Rcの筒状内周
面を持つ渦流室用内周壁21を水平中間壁52上に形成
し、前記鉛直中心線と同心に配置し、上方から降下挿入
するインペラーシャフト61の下端に前記最小動径Rb
より若干短い半径Raの円板62を設けると共に該円板
62上に羽根63を立設してインペラー60を形成し、
且つインペラー60を最下位置に上方から挿入したとき
円板62下面とポンプハウジングの底42との間に若干
の間隔Hを保つ如く面も水平中間壁52下面と羽根63
上面とが略同一面になる如く構成し、また渦流室20の
周壁21よりも上位で変化する溶湯面11の上限11
d,下限11e間の位置に応じて溶湯面11が高いとき
にはインペラーシャフト61の回転速度を速くし、溶湯
面が低いときにはインペラーシャフト61の回転速度を
遅くする回転速度制御装置8を備えている。
The present invention is directed to a burner 31.
9d of the molten metal heating chamber 30 having the above is taken out and passed through the upper open swirl chamber 20.
In a circulation type non-ferrous metal melting furnace configured so that the low temperature molten metal 9e having melted 0 and lowered in temperature is again introduced into the molten metal heating chamber 30 to raise the temperature, the inner wall 41 of the pump housing 40 having the bottom 42 formed in a horizontal plane is represented by polar coordinates. When viewed, the radius vector Rx rotates around the pole Q and the minimum radius vector Rb slightly longer than the radius Ra of the impeller is used as the starting point Pb. Vertical side walls 44 and 45 of the discharge port 43 are constituted by a tangent line Sd extending from the end point Pd of the vortex line having the same diameter Rd and a line Sb gradually increasing the distance from the starting point Pb with respect to the tangent line Sd. A horizontal intermediate wall 52 having a circular hole 51 centered on a vertical center line passing through the pole Q and having the same radius as the minimum radius vector Rb is formed on the pump housing 40 and is larger than the minimum radius vector Rb of the vortex line. Maximum motion An inner peripheral wall 21 for a swirl chamber having a cylindrical inner peripheral surface having a radius Rc smaller than Rd is formed on a horizontal intermediate wall 52, is arranged concentrically with the vertical center line, and is provided at the lower end of an impeller shaft 61 which is descended and inserted from above. The minimum radius Rb
A disc 62 having a slightly shorter radius Ra is provided, and blades 63 are provided upright on the disc 62 to form an impeller 60.
Moreover, when the impeller 60 is inserted into the lowermost position from above, a slight gap H is maintained between the lower surface of the disk 62 and the bottom 42 of the pump housing.
The upper surface of the molten metal 11 is configured to be substantially flush with the upper surface, and the upper limit 11 of the molten metal surface 11 changes above the peripheral wall 21 of the swirl chamber 20.
According to the position between d and the lower limit 11e, the rotation speed control device 8 is provided to increase the rotation speed of the impeller shaft 61 when the molten metal surface 11 is high, and to decrease the rotation speed of the impeller shaft 61 when the molten metal surface is low.

【0006】[0006]

【実施例】実施例について図面によって説明すると、2
0は上方から供給した金属屑10を高温溶湯9dに巻込
んで下方に導く略直立円筒状渦流室であって、その上部
を高温溶湯9dが流入可能に開口してあり、下部には水
平中間壁52を隔て、接線方向に吐出口43を備えたポ
ンプハウジング40を設け、且つそのポンプハウジング
40には渦流を形成するところの水平円板62上に複数
枚の羽根63を放射状に取付けたインペラー60を配置
してある。30は溶湯加熱室であって、高温溶湯9dに
浸漬する部分は下方に向かって幅が広くなるよう、逆テ
ーパー状に形成してあり、上方に高温溶湯9dを加熱す
るバーナー31を設けてあり、また渦流室20とは堰1
2により隔てられているが、渦流室20とは湯面下方で
連通している。13は溶湯加熱室30から前記渦流室2
0上部に高温溶湯9dを導く湯道であって、溶湯加熱室
30との境に上方から高温溶湯9d中に湯面に浮遊した
スラグの進入を阻止する上下動可能にスラグスクレーパ
ー14を挿入してある。上記渦流室20、溶湯加熱室3
0及び湯道13は、耐火物壁15で隔てられてはいる
が、全体として耐火物壁15で囲まれていて、一体化さ
れており、溶湯加熱室30の一方の側に渦流室20及び
湯道13を並べて配置し、他方の側に運転保守用の扉1
6を設け、溶湯循環路を形成してある。その他、17は
上下動可能なインペラー駆動用モーター、22は金属屑
供給コンベヤーである。また、18は溶湯レベル計であ
って、溶湯レベルを最適に制御可能にしてあると共に、
溶湯レベルによって最適の渦形状を形成するようインペ
ラー60の回転速度を回転速度制御装置8を介して制御
可能にしてある。
BRIEF DESCRIPTION OF THE DRAWINGS FIG.
Reference numeral 0 denotes a substantially vertical cylindrical swirl chamber in which the metal scrap 10 supplied from above is wound around the high-temperature molten metal 9d and guided downward, the upper part of which is opened so that the high-temperature molten metal 9d can flow in, and the lower part has a horizontal middle portion. An impeller in which a pump housing 40 having a discharge port 43 in a tangential direction is provided with a wall 52 therebetween, and a plurality of blades 63 are radially mounted on a horizontal disk 62 where a vortex is formed in the pump housing 40. 60 are arranged. Reference numeral 30 denotes a molten metal heating chamber, which is formed in a reverse taper shape so that a portion to be immersed in the high temperature molten metal 9d becomes wider downward, and a burner 31 for heating the high temperature molten metal 9d is provided above. Also, the swirl chamber 20 is the weir 1
They are separated by 2, but communicate with the swirl chamber 20 below the molten metal surface. Reference numeral 13 denotes the molten metal heating chamber 30 to the swirl chamber 2
0 is a runner that guides the high-temperature molten metal 9d to the upper part, and a slag scraper 14 is inserted into the high-temperature molten metal 9d from the upper side at the boundary with the molten-metal heating chamber 30 so that the slag scraper 14 can be vertically moved to prevent the slag floating on the molten metal surface from entering. There is. The swirl chamber 20 and the molten metal heating chamber 3
0 and the runway 13 are separated by the refractory wall 15, but are surrounded by the refractory wall 15 as a whole and integrated, and the swirl chamber 20 and the swirl chamber 20 are provided on one side of the molten metal heating chamber 30. The runners 13 are arranged side by side, and the door 1 for operation and maintenance is provided on the other side.
6 is provided to form a molten metal circulation path. In addition, 17 is an up-and-down movable motor for driving the impeller, and 22 is a metal scrap supply conveyor. Further, 18 is a molten metal level meter, which enables the molten metal level to be optimally controlled, and
The rotation speed of the impeller 60 can be controlled via the rotation speed control device 8 so as to form an optimum vortex shape depending on the molten metal level.

【0007】投入した金属屑10を渦流によって溶解す
る本発明の要部について詳細に説明する。
The essential part of the present invention for melting the thrown metal scrap 10 by a vortex will be described in detail.

【0008】底42を水平面に形成したポンプハウジン
グ40の内壁41を極座標でみたとき動径Rxが極Qの
周わりを回動すると共にインペラーの半径Raより僅か
に長い最小動径Rbを始点Pbとし、極Qから徐々に遠
ざかる点が画く渦線で形成し、且つ最大同径Rdの渦線
の終点Pdから延びる接線Sdと、該接線Sdに対し前
記始点Pbから徐々に間隔を広げる直線Sbとで以って
吐出口43の垂直両側壁44,45を構成してある。
When the inner wall 41 of the pump housing 40 having the bottom 42 formed in a horizontal plane is viewed in polar coordinates, the radius vector Rx rotates around the pole Q and the minimum radius vector Rb slightly longer than the radius Ra of the impeller is set as the starting point Pb. A tangent line Sd extending from the end point Pd of the vortex line having the maximum diameter Rd, and a straight line Sb gradually increasing the distance from the starting point Pb to the tangent line Sd. Thus, the vertical side walls 44 and 45 of the discharge port 43 are formed.

【0009】極Qを通る鉛直中心線を中心とし且つ前記
最小動径Rbと同一半径の円孔51を有する水平中間壁
52をポンプハウジング40上に形成してある。
A horizontal intermediate wall 52 having a circular hole 51 centered on a vertical center line passing through the pole Q and having the same radius as the minimum radius vector Rb is formed on the pump housing 40.

【0010】渦線の最小動径Rbより大きく且つ最大動
径Rdより小さい半径Rcの筒状内周面を持つ渦流室用
内周壁21を形成してある。
An inner peripheral wall 21 for a swirl chamber is formed having a cylindrical inner peripheral surface having a radius Rc which is larger than the minimum radius Rb of the vortex line and smaller than the maximum radius Rd.

【0011】前記鉛直中心線と同心に配置し、上方から
降下挿入するインペラーシャフト61の下端に前記最小
動径Rbより若干短い半径Raの円板62を設けると共
に該円板62上に羽根63を立設してインペラー60を
形成し、且つインペラー60を最下位置に上方から挿入
したとき円板62下面とポンプハウジングの底42との
間に若干の間隔Hを保つ如く而も水平中間壁52下面と
羽根63上面とが略同一面になる如く構成してある。
A disc 62 having a radius Ra slightly shorter than the minimum moving radius Rb is provided at the lower end of an impeller shaft 61 which is arranged concentrically with the vertical center line and is inserted downward from above, and blades 63 are provided on the disc 62. The impeller 60 is erected vertically, and when the impeller 60 is inserted from the uppermost position to the lowermost position, a horizontal space 52 is formed so as to maintain a slight distance H between the lower surface of the disk 62 and the bottom 42 of the pump housing. The lower surface and the upper surface of the blade 63 are configured to be substantially flush with each other.

【0012】また渦流室20の内周壁21よりも上位で
変化する溶湯面11の上限11d,下限11e間の位置
に応じて溶湯面11が高いときにはインペラーシャフト
61の回転速度を速くし、溶湯面が低いときにはインペ
ラーシャフト61の回転速度を遅くする回転速度制御装
置8が設けてある。
Further, when the molten metal surface 11 is high depending on the position between the upper limit 11d and the lower limit 11e of the molten metal surface 11 which changes above the inner peripheral wall 21 of the swirl chamber 20, the rotation speed of the impeller shaft 61 is increased to increase the molten metal surface. There is provided a rotation speed control device 8 for slowing the rotation speed of the impeller shaft 61 when is low.

【0013】作用について説明すると、先ず扉16を開
けて、金属屑と同じ金属材を適当量挿入し、バーナー3
1により加熱、金属材を溶解し、溶湯を調製する。続い
て、モーター17を起動し、インペラー60を回転させ
ると、そのポンプ作用により、吐出口43,堰12,溶
湯加熱室30,湯道13,渦流室20,インペラー60
を巡る溶湯循環路が形成される。そして金属屑10は上
開渦流室20へ向って投入され、インペラー60を通過
するときには殆ど溶解してており、インペラーを傷つけ
ない。
The operation will be described. First, the door 16 is opened and the same metal material as the metal scrap is inserted into the burner 3
In step 1, heating is performed to melt the metal material and prepare a molten metal. Subsequently, when the motor 17 is started and the impeller 60 is rotated, the pump action thereof causes the discharge port 43, the weir 12, the molten metal heating chamber 30, the runner 13, the swirl chamber 20, and the impeller 60.
A molten metal circulation path is formed. Then, the metal scrap 10 is thrown into the upper open swirl chamber 20 and is almost melted when passing through the impeller 60, so that the impeller is not damaged.

【0014】[0014]

【発明の効果】本発明は、バーナー31を備えた溶湯加
熱室30の高温溶湯9dを取出して金属屑10を投入す
る上開渦流室20を通過させ、該渦流室20において金
属屑10を溶かして温度の下がった低温溶湯9eを再び
溶湯加熱室30に導いて昇温する如く構成した循環型非
鉄金属溶解炉において、溶湯レベル計18により溶湯レ
ベルを検出し、最適に制御可能ににしてあると共に、溶
湯レベルによって最適の渦形状を形成するようインペラ
ー60の回転速度を制御可能にしてあり、供給された金
属屑10を瞬時に渦に巻込み、溶解することができ、歩
留まりよく、且つ熱効率よく、再生回収することが可能
であり、渦流室20及びインペラー60の構造も簡単
で、損傷し難く、寿命も長く、保守負担が著しく軽減さ
れる。
According to the present invention, the high temperature molten metal 9d in the molten metal heating chamber 30 equipped with the burner 31 is taken out and passed through the upper open swirl chamber 20 into which the metal scrap 10 is introduced, and the metal scrap 10 is melted in the swirl chamber 20. In the circulation type non-ferrous metal melting furnace configured to guide the temperature of the low temperature molten metal 9e, whose temperature has been lowered, to the molten metal heating chamber 30 again to raise the temperature, the molten metal level meter 18 detects the molten metal level to enable optimum control. At the same time, the rotation speed of the impeller 60 can be controlled so as to form an optimum vortex shape depending on the level of the molten metal, and the supplied metal scrap 10 can be instantly wound into the vortex and melted, resulting in good yield and thermal efficiency. Well, it can be recycled and recovered, and the structures of the swirl chamber 20 and the impeller 60 are simple, they are hard to be damaged, have a long life, and the maintenance load is remarkably reduced.

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

【図1】本発明の実施例を示す一部切欠垂直切断正面図
である。
FIG. 1 is a partially cutaway vertical cut front view showing an embodiment of the present invention.

【図2】図1のH−H切断一部省略平面図である。FIG. 2 is a plan view of the HH section of FIG.

【図3】図1のJ−J切断一部省略側面図である。FIG. 3 is a side view of the JJ section of FIG.

【図4】要部の拡大平面図である。FIG. 4 is an enlarged plan view of a main part.

【図5】要部の拡大正面図である。FIG. 5 is an enlarged front view of a main part.

【図6】図5のK−K底面図である。FIG. 6 is a bottom view of KK in FIG.

【符号の説明】[Explanation of symbols]

8 回転速度制御装置 9d 高温溶湯 9e 低温溶湯 10 金属屑 11 溶湯面 11d 溶湯面の上限 11e 溶湯面の下限 12 堰 13 湯道 14 スラグスクレーパー 15 耐火物壁 16 扉 17 モーター 18 レベル計 19 温度計 20 渦流室 21 渦流室の内周壁 22 金属屑供給コンベヤー 30 溶湯加熱室 31 バーナー 40 ポンプハウジング 41 ポンプハウジングの内壁 42 ポンプハウジングの底 43 吐出口 44 渦線の終点から始まる吐出口の側壁 45 渦線の始点から始まる吐出口の側壁 51 円孔 52 水平中間壁 60 インペラー 61 インペラーシャフト 62 円板 63 羽根 H 円板とポンプハウジングの底との間隙 Pb 渦線の始点 Pd 渦線の終点 Q 極 Ra 円板の半径 Rb 渦線の最小動径 Rc 渦流室の内周壁の半径 Rd 渦線の最大動径 Rx 動径 Sb 渦線の始点から始まる直線 Sd 渦線の終点の接線 8 Rotation speed control device 9d High temperature molten metal 9e Low temperature molten metal 10 Metal scrap 11 Molten metal surface 11d Upper limit of molten metal surface 11e Lower limit of molten metal surface 12 Weir 13 Runway 14 Slag scraper 15 Refractory wall 16 Door 17 Motor 18 Level meter 19 Thermometer 20 Vortex chamber 21 Inner wall of vortex chamber 22 Metal scrap supply conveyor 30 Molten metal heating chamber 31 Burner 40 Pump housing 41 Pump housing inner wall 42 Pump housing bottom 43 Discharge port 44 Discharge port side wall starting from the end of vortex line 45 Vortex line Side wall of discharge port starting from the starting point 51 Circular hole 52 Horizontal intermediate wall 60 Impeller 61 Impeller shaft 62 Disc 63 Blade H H Gap between disc and bottom of pump housing Pb Start point of vortex line Pd End point of vortex line Q pole Ra disc Radius Rb Minimum radius of vortex line Rc Radius of inner wall of vortex chamber Tangent of the end point of the straight line Sd vortex line starting from the start point of the maximum radius Rx radius Sb vortex line d circumvolution

───────────────────────────────────────────────────── フロントページの続き (72)発明者 田尻 昇 広島県広島市中区東千田町1丁目1番72号 三建産業株式会社内 (72)発明者 奥田 時良 愛知県刈谷市朝日町2丁目1番地アイシン 精機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Noboru Tajiri 1-12-1 Higashisenta-cho, Naka-ku, Hiroshima-shi, Hiroshima Sanken Sangyo Co., Ltd. (72) Tokura Okuda 2 Asahi-cho, Kariya, Aichi 1-chome Aisin Seiki Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 バーナー(31)を備えた溶湯加熱室
(30)の高温溶湯(9d)を取出して上開渦流室(2
0)を通過させ、該渦流室(20)において金属屑(1
0)を溶かして温度の下がった低温溶湯(9e)を再び
溶湯加熱室(30)に導いて昇温する如く構成した循環
型非鉄金属溶解炉において、 底(42)を水平面に形成したポンプハウジング(4
0)の内壁(41)を極座標でみたとき動径(Rx)が
極(Q)の周わりを回動すると共にインペラーの半径
(Ra)より僅かに長い最小動径(Rb)を始点(P
b)とし、極(Q)から徐々に遠ざかる点が画く渦線で
形成し、且つ最大動径(Rd)の渦線の終点(Pd)か
ら延びる接線(Sd)と、該接線(Sd)に対し前記始
点(Pb)から徐々に間隔を広げる線(Sb)とで以っ
て吐出口(43)の垂直両側壁(44,45)を構成
し、 前記極(Q)を通る鉛直中心線を中心とし且つ前記最小
動径(Rb)と同一半径の円孔(51)を有する水平中
間壁(52)をポンプハウジング(40)上に形成し、 前記渦線の最小動径(Rb)より大きく且つ最大動径
(Rd)より小さい半径(Rc)の筒状内周面を持つ渦
流室用内周壁(21)を水平中間壁(52)上に形成
し、 前記鉛直中心線と同心に配置し、上方から降下挿入する
インペラーシャフト(61)の下端に前記最小動径(R
b)より若干短い半径(Ra)の円板(62)を設ける
と共に該円板(62)上に羽根(63)を立設してイン
ペラー(60)を形成し、且つインペラー(60)を最
下位置に上方から挿入したとき円板(62)下面とポン
プハウジングの底(42)との間に若干の間隙(H)を
保つ如く而も水平中間壁(52)下面と羽根(63)上
面とが略同一面になる如く構成し、 また渦流室(20)の内周壁(21)よりも上位で変化
する溶湯面(11)の上限(11d),下限(11e)
間の位置に応じて溶湯面(11)が高いときにはインペ
ラーシャフト(61)の回転速度を速くし、溶湯面が低
いときにはインペラーシャフトの回転速度を遅くする回
転速度制御装置(8)を備えたことを特徴とする循環型
非鉄金属溶解炉。
1. A high-temperature molten metal (9d) in a molten metal heating chamber (30) equipped with a burner (31) is taken out to form an upper open swirl chamber (2).
0), and the metal scrap (1
In a circulation type non-ferrous metal melting furnace configured so that the low temperature molten metal (9e) which is melted from (0) and is cooled down is introduced again to the molten metal heating chamber (30) to raise the temperature, a pump housing having a bottom (42) formed in a horizontal plane. (4
When the inner wall (41) of (0) is viewed in polar coordinates, the radius vector (Rx) rotates around the pole (Q) and the minimum radius vector (Rb) slightly longer than the radius (Ra) of the impeller is set as the starting point (P
b), a tangential line (Sd) extending from the end point (Pd) of the vortex line having the maximum radius vector (Rd), and the tangent line (Sd). On the other hand, a line (Sb) gradually increasing the distance from the starting point (Pb) constitutes vertical side walls (44, 45) of the discharge port (43), and a vertical center line passing through the pole (Q) is formed. A horizontal intermediate wall (52) having a circular hole (51) as a center and having the same radius as the minimum radius vector (Rb) is formed on the pump housing (40) and is larger than the minimum radius vector (Rb) of the vortex line. An inner peripheral wall (21) for a swirl chamber having a cylindrical inner peripheral surface having a radius (Rc) smaller than the maximum radius vector (Rd) is formed on the horizontal intermediate wall (52) and arranged concentrically with the vertical center line. , The lower limit of the radial vector (R
b) A disc (62) having a radius (Ra) slightly shorter than that of b) is provided, and the vanes (63) are erected on the disc (62) to form an impeller (60). The lower surface of the horizontal intermediate wall (52) and the upper surface of the blades (63) are maintained so that a slight gap (H) is maintained between the lower surface of the disc (62) and the bottom (42) of the pump housing when inserted from above into the lower position. And the upper surface (11d) of the molten metal surface (11) and the lower limit (11e) of the molten metal surface (11) that change above the inner peripheral wall (21) of the swirl chamber (20).
A rotation speed control device (8) for increasing the rotation speed of the impeller shaft (61) when the molten metal surface (11) is high, and for decreasing the rotation speed of the impeller shaft when the molten metal surface is low. A circulating type non-ferrous metal melting furnace.
JP4631492A 1992-01-31 1992-01-31 Circulating non-ferrous metal scrap melting furnace Expired - Lifetime JPH0820181B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4631492A JPH0820181B2 (en) 1992-01-31 1992-01-31 Circulating non-ferrous metal scrap melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4631492A JPH0820181B2 (en) 1992-01-31 1992-01-31 Circulating non-ferrous metal scrap melting furnace

Publications (2)

Publication Number Publication Date
JPH05214457A JPH05214457A (en) 1993-08-24
JPH0820181B2 true JPH0820181B2 (en) 1996-03-04

Family

ID=12743710

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4631492A Expired - Lifetime JPH0820181B2 (en) 1992-01-31 1992-01-31 Circulating non-ferrous metal scrap melting furnace

Country Status (1)

Country Link
JP (1) JPH0820181B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004257715A (en) * 2003-02-27 2004-09-16 Nippon Kounetsu Kogyosha:Kk Metal melting holding furnace
KR101966205B1 (en) * 2017-08-28 2019-04-05 (주)디에스리퀴드 Aluminum melting furnace
KR101966206B1 (en) * 2017-08-28 2019-04-05 (주)디에스리퀴드 Aluminum melting furnace

Also Published As

Publication number Publication date
JPH05214457A (en) 1993-08-24

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