JPH0413598Y2 - - Google Patents
Info
- Publication number
- JPH0413598Y2 JPH0413598Y2 JP1985073146U JP7314685U JPH0413598Y2 JP H0413598 Y2 JPH0413598 Y2 JP H0413598Y2 JP 1985073146 U JP1985073146 U JP 1985073146U JP 7314685 U JP7314685 U JP 7314685U JP H0413598 Y2 JPH0413598 Y2 JP H0413598Y2
- Authority
- JP
- Japan
- Prior art keywords
- nozzle
- opening
- molten metal
- pump cylinder
- furnace
- 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
Links
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は金属溶湯攪拌装置のノズル開口部構造
に関する。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a nozzle opening structure for a molten metal stirring device.
(従来の技術)
アルミニウム、銅、亜鉛などの金属溶湯炉では
溶湯を攪拌しない場合、溶融時間が長くなり、加
熱すべき温度が高くなる外に、酸化物の発生量が
多くなる。このため、上記溶湯を攪拌することに
よつて、酸化物の発生量、溶融時間ともに約10%
減少させることが認められている。(Prior Art) In a furnace for melting metals such as aluminum, copper, and zinc, if the molten metal is not stirred, the melting time becomes longer, the temperature to be heated becomes higher, and the amount of oxides generated increases. Therefore, by stirring the above molten metal, both the amount of oxide generated and the melting time can be reduced by approximately 10%.
It is recognized that it can be reduced.
第3図は周知の機械的攪拌装置の構成図であ
る。同図において、溶融炉1の下側下部にノズル
2を内設した耐火物よりなる中間体3を設け、該
中間体3に内壁を耐火材料で内張りしたポンプシ
リンダ4を取付ける。該ポンプシリンダ4はノズ
ル2を介して溶融炉1の内底部と連通すると共
に、該ポンプシリンダ4の上端部は、中間に外気
と負圧との自動切換バルブ5、サイクロン6、フ
イルタ7等を介在した通気管8により真空ブロワ
9と接続されている。該真空ブロワ9はモータ1
0によつて作動し、ポンプシリンダ4内に真空負
圧によつて溶湯を吸引導入し、一定時間経過後に
自動切換バルブ5を切換えて外気をシリンダ内に
導入する。真空吸引力を抜いて外気を導入したの
で、ポンプシリンダ4内に吸い上げられた溶湯は
自重で溶融炉1内に戻ることにより、該炉内に滞
留した溶湯に対流が生じ、溶融炉1内は攪拌され
る。 FIG. 3 is a block diagram of a known mechanical stirring device. In the figure, an intermediate body 3 made of a refractory material and having a nozzle 2 therein is provided at the bottom of a melting furnace 1, and a pump cylinder 4 whose inner wall is lined with a refractory material is attached to the intermediate body 3. The pump cylinder 4 communicates with the inner bottom of the melting furnace 1 through the nozzle 2, and the upper end of the pump cylinder 4 is provided with an automatic switching valve 5 between outside air and negative pressure, a cyclone 6, a filter 7, etc. in the middle. It is connected to a vacuum blower 9 by an intervening vent pipe 8. The vacuum blower 9 has a motor 1
0, the molten metal is sucked into the pump cylinder 4 by vacuum negative pressure, and after a certain period of time, the automatic switching valve 5 is switched to introduce outside air into the cylinder. Since the vacuum suction force was removed and outside air was introduced, the molten metal sucked up into the pump cylinder 4 returns to the melting furnace 1 by its own weight, causing convection in the molten metal staying in the furnace, and the inside of the melting furnace 1 Stirred.
(考案が解決しようとする問題点)
溶融作業を終えた例えばアルミニウムの溶湯が
溶融炉1内に所定量残して排出され、新しい冷材
が該炉内に加えらえ、ポンプシリンダ4の吸引・
吐出作業が再開される場合を考える。溶融炉1内
に冷材が加えられると、炉内の表面溶融物は約
1000℃近くの温度であるのに、冷材の一部分は50
℃位のように温度むらが大きい。ポンプシリンダ
4が作動を開始すると、冷材はポンプシリンダ4
から排出される溶湯を浴びて温度上昇し、溶融が
促進される。同時に、溶湯の波動効果によつて溶
融炉1内の溶湯温度も均一化される。このため、
冷材を早く溶融させる観点からは、吸引溶湯エネ
ルギー損失を抑制し、攪拌効率を高めると共に、
早い時点でのポンプシリンダ4の作動開始が望ま
しい。(Problem to be solved by the invention) After the melting process, for example, molten aluminum is discharged leaving a predetermined amount in the melting furnace 1, new coolant is added to the furnace, and the suction of the pump cylinder 4 is carried out.
Consider the case where the dispensing work is restarted. When cold material is added into the melting furnace 1, the surface melt inside the furnace is approximately
Even though the temperature is close to 1000℃, a part of the refrigerant has a temperature of 50℃.
There are large temperature fluctuations, such as around ℃. When the pump cylinder 4 starts operating, the cold material flows into the pump cylinder 4.
The temperature rises due to the molten metal discharged from the tank, promoting melting. At the same time, the temperature of the molten metal in the melting furnace 1 is also made uniform due to the wave effect of the molten metal. For this reason,
From the perspective of melting the cold material quickly, it is possible to suppress the energy loss of suction molten metal, increase the stirring efficiency, and
It is desirable to start operating the pump cylinder 4 at an early point in time.
しかるに、上記早い時点では、炉内の溶湯レベ
ルが炉壁に下部縁が炉床面と同一面になるように
形成されたノズル2の開口部2aよりあまり高く
ない状態である。もし上記溶湯レベルが開口部2
aより低い場合にポンプシリンダ4に溶湯の他に
炉内の空気をも吸込み、この吸込まれた空気はポ
ンプシリンダ4内で溶湯を酸化させるという問題
点があつた。 However, at this early point in time, the molten metal level in the furnace is not much higher than the opening 2a of the nozzle 2 formed in the furnace wall so that its lower edge is flush with the hearth surface. If the above molten metal level is at opening 2
When the temperature is lower than a, there is a problem in that the air in the furnace is sucked into the pump cylinder 4 in addition to the molten metal, and this sucked air oxidizes the molten metal in the pump cylinder 4.
(問題点を解決するための手段)
本考案は上記問題点を解決するために、溶融炉
1の壁面に形成されるノズル2の開口部2aの開
口面積は、上記ポンプシリンダ4の下部端面の開
孔部断面積と等しく、且つノズルの開口部2aは
下部縁が炉床面と同一面になるようにされ、しか
も開口部2aの形状は溶融炉1の深さ方向寸法が
幅方向寸法より短く選定されると共に、このノズ
ルは溶湯を水平方向に吐出させるに足り、且つ炉
壁の厚みより短い寸法のノズル水平部分と、上記
ポンプシリンダに連通するノズル傾斜部分とを有
するように構成したことを特徴とする。(Means for Solving the Problems) In order to solve the above-mentioned problems, the present invention has an aim that the opening area of the opening 2a of the nozzle 2 formed on the wall surface of the melting furnace 1 is smaller than that of the lower end surface of the pump cylinder 4. The cross-sectional area of the opening 2a is equal to the cross-sectional area of the opening, and the lower edge of the opening 2a of the nozzle is flush with the hearth surface, and the shape of the opening 2a is such that the depth direction dimension of the melting furnace 1 is larger than the width direction dimension. In addition to being selected to be short, this nozzle is configured to have a horizontal nozzle portion that is sufficient to discharge the molten metal in a horizontal direction and that is shorter than the thickness of the furnace wall, and an inclined nozzle portion that communicates with the pump cylinder. It is characterized by
(作用)
本考案は上記の構成によつて、下部縁が炉床面
と同一面になるように形成したノズル開口部2a
の溶融炉1の深さ方向寸法は、従来の真円形ノズ
ル開口部の直径より短く、しかも開口面積は従来
方式のと同一となる。従つて、本考案では従来方
式に比べて、溶融炉1の溶湯の他に空気をも吸込
む溶湯レベルが低くなるので、ポンプシリンダ4
の作動開始が早くなる。(Function) The present invention has the above-described structure, and the nozzle opening 2a is formed so that the lower edge is flush with the hearth surface.
The depth dimension of the melting furnace 1 is shorter than the diameter of the conventional perfectly circular nozzle opening, and the opening area is the same as that of the conventional method. Therefore, in the present invention, the level of molten metal that sucks air in addition to the molten metal in the melting furnace 1 is lower than that in the conventional method, so the pump cylinder 4
starts operating faster.
(実施例)
以下、本考案の実施例を図面を参照して説明す
る。第1図は本実施例に係る溶融炉に連通するノ
ズルの図面で、図Aは縦断正面図、図Bは図Aの
直線20−20の断面図、図Cは図Aの直線21
−21の断面図であり、第2図Aはポンプシリン
ダの縦断正面図、第2図Bはポンプシリンダの平
面図である。なお、第1図、第2図では、従来方
式の構成を示す第3図と同一である部分は同一符
号を付与する。(Example) Hereinafter, an example of the present invention will be described with reference to the drawings. Figure 1 is a diagram of a nozzle communicating with the melting furnace according to this embodiment, where Figure A is a vertical front view, Figure B is a sectional view taken along straight line 20-20 in Figure A, and Figure C is a straight line 21 in Figure A.
-21, FIG. 2A is a longitudinal sectional front view of the pump cylinder, and FIG. 2B is a plan view of the pump cylinder. Note that in FIGS. 1 and 2, parts that are the same as those in FIG. 3 showing the configuration of the conventional system are given the same reference numerals.
第2図に示されるように、ポンプシリンダ4の
溶湯を吸い上げ、吐き出す中空孔部4aの断面形
状は、上端部4bから下端部4cまで一定の真円
形である。これに対し、ノズル2については、第
3図に示す如く、下部縁が溶融炉1の炉床1aと
同一面になるようにこの炉壁1に形成されるノズ
ルの開口部2aは、第1図A,Bに示す如く、矩
形状であつて、溶融炉1の深さ方向寸法Lが横幅
寸法Mより短く形成される。他方、該ノズル2の
ポンプシリンダ4の下部端面上の開孔部2bは、
第1図Cに示されるように真円形で、この真円形
の面積は開口部2aの断面積と同一であると共
に、第2図に示したポンプシリンダ4の中空孔部
4aの断面積と同一面積を有している。従つて、
ノズル2は開口部2aでは断面矩形であり、この
開口部2aからポンプ4の下部端面の開孔部2b
に向う弯曲部2cまでの間で、上記矩形から真円
になだらかな曲線を有して変形される。 As shown in FIG. 2, the hollow hole 4a of the pump cylinder 4 that sucks up and discharges the molten metal has a constant perfect circular cross-sectional shape from the upper end 4b to the lower end 4c. On the other hand, as for the nozzle 2, as shown in FIG. As shown in FIGS. A and B, the melting furnace 1 has a rectangular shape, and the depth dimension L of the melting furnace 1 is shorter than the width dimension M. On the other hand, the opening 2b on the lower end surface of the pump cylinder 4 of the nozzle 2 is
As shown in FIG. 1C, it is a perfect circle, and the area of this perfect circle is the same as the cross-sectional area of the opening 2a and the cross-sectional area of the hollow hole 4a of the pump cylinder 4 shown in FIG. It has an area. Therefore,
The nozzle 2 has a rectangular cross section at the opening 2a, and extends from the opening 2a to the opening 2b in the lower end face of the pump 4.
The shape is transformed from the rectangular shape to a perfect circle with a gentle curve up to the curved portion 2c.
次に動作を説明する。溶融炉1内の冷材が攪拌
作用によつて溶融し、溶湯が炉内にノズル2の開
口部2aを満たす程度の所定量を残して炉外に排
出され、新しい冷材が溶融炉1内に加えられる。
次いで、モータ10を起動してポンプシリンダ4
内を真空とし、溶融炉1内の溶湯を、該溶湯のレ
ベルがノズル2の開口部2aより高い程度となる
ように少量をポンプシリンダ4内に吸い上げ、そ
の後吐出させる。この攪拌作業を繰り返すと、炉
内の冷材は上記吐出された溶湯を浴びて溶融が促
進されると共に、炉内の溶湯の温度が均一化され
る。 Next, the operation will be explained. The cold material in the melting furnace 1 is melted by the stirring action, and the molten metal is discharged from the furnace leaving a predetermined amount that is enough to fill the opening 2a of the nozzle 2 in the furnace, and new cold material is poured into the melting furnace 1. added to.
Next, the motor 10 is started to operate the pump cylinder 4.
A vacuum is created inside the melting furnace 1, and a small amount of the molten metal in the melting furnace 1 is sucked up into the pump cylinder 4 so that the level of the molten metal is higher than the opening 2a of the nozzle 2, and then discharged. By repeating this stirring operation, the cold material in the furnace is bathed in the discharged molten metal, which promotes melting and equalizes the temperature of the molten metal in the furnace.
また、ノズル2は矩形状の開口部2aから該ノ
ズルの弯曲部2cまでなだらかな曲線を描いて断
面真円形となり、その後ポンプシリンダ4の下部
端面の開孔部2bまで真円形を保持する。しかも
この真円形はポンプシリンダ4の中空孔部4aと
同一面積を有するので、従来方式の開口部が真円
形ノズルの場合と攪拌作用に差異がない。 Further, the nozzle 2 draws a gentle curve from the rectangular opening 2a to the curved part 2c of the nozzle to have a perfect circular cross section, and then maintains a perfect circular shape until the opening 2b of the lower end face of the pump cylinder 4. Moreover, since this perfect circle has the same area as the hollow hole 4a of the pump cylinder 4, there is no difference in stirring action from the case where the opening of the conventional system is a perfect circular nozzle.
なお、本実施例ではノズルの開口部2aを真円
と同一面積を有する深さ寸法の小さい矩形状とし
たが、これに限定されるものではなく、真円と同
一面積を有すると共に、深さ寸法が真円の直径よ
り小さい例えば楕円形状などであつてもよい。 In this embodiment, the opening 2a of the nozzle is formed into a rectangular shape having the same area as a perfect circle and a small depth, but is not limited to this. For example, the shape may be an ellipse whose size is smaller than the diameter of a perfect circle.
(考案の効果)
以上説明のように、本考案は溶融炉の炉壁に下
部縁が炉床面と同一面となるように形成されたポ
ンプシリンダに連通するノズルの開口部の面積
を、上記ポンプシリンダの下部端面の開孔部面積
即ちポンプシリンダの真円形中空孔部断面積と同
一とすると共に、上記開口部の形状を溶融炉の深
さ方向の寸法が横幅寸法より短く形成し、さらに
はノズル水平部分の寸法を溶湯を水平方向に吐出
させるに足り、且つ、炉壁の厚みより短くし、該
ノズル水平部分とポンプシリンダ間を最短距離の
傾斜部分で構成したので、下記の効果がある。す
なわち攪拌作業による冷材の溶湯排出後、新しく
炉内に挿入された冷材の攪拌作業の再開に際し、
従来方式ではノズル開口部が真円形であるため、
該開口部に溶湯が充満しポンプシリンダにより溶
湯を吸込んでも空気の同時吸入がない時点までポ
ンプ作動を見合わせなければならなかつたが、本
考案のノズルによれば、空気を吸込むおそれが少
なく、それに伴つて、吸込んだ空気によつて溶湯
を酸化させることがないので、攪拌のスタートが
早くできると共に、溶湯吐出流のエネルギー損失
を抑制し、ノズルからの噴流を水平方向に、より
遠方にまで到達するようにし、または炉内の冷材
に衝突させてその溶融を促進させることができ、
結局、溶融効率を高め、溶融時間を短縮すること
ができ、燃費の大幅な節約および歩留向上効果が
顕著である。(Effects of the invention) As explained above, the present invention has the area of the opening of the nozzle communicating with the pump cylinder, which is formed on the furnace wall of the melting furnace so that its lower edge is flush with the hearth surface, as described above. The area of the opening in the lower end face of the pump cylinder is the same as the cross-sectional area of the perfectly circular hollow hole of the pump cylinder, and the shape of the opening is such that the dimension in the depth direction of the melting furnace is shorter than the width dimension, and The size of the horizontal nozzle part is sufficient to discharge the molten metal horizontally and is shorter than the thickness of the furnace wall, and the horizontal part of the nozzle and the pump cylinder are configured with an inclined part with the shortest distance, so the following effects can be achieved. be. In other words, after the cold material has been discharged from the molten metal by stirring work, when the stirring work of the cold material newly inserted into the furnace is restarted,
In the conventional method, the nozzle opening is perfectly circular, so
Previously, pump operation had to be suspended until the opening was filled with molten metal and air was not sucked in at the same time even if the molten metal was sucked into the pump cylinder.However, with the nozzle of the present invention, there is less risk of sucking in air; At the same time, since the molten metal is not oxidized by the sucked air, stirring can be started quickly, energy loss in the molten metal discharge flow is suppressed, and the jet from the nozzle can reach further distances in a horizontal direction. or collide with the cold material in the furnace to accelerate its melting.
As a result, the melting efficiency can be increased and the melting time can be shortened, resulting in significant fuel savings and yield improvement effects.
第1図、第2図は本考案の実施例に関する図面
で、第1図Aはノズルの縦断正面図、図Bは図A
の矢印20−20断面図、図Cは図Aの矢印21
−21断面図、第2図Aはポンプシリンダの縦断
正面図、図Bはポンプシリンダの平面図、第3図
は周知の機械的攪拌装置の構成図である。
1……溶融炉、2……ノズル、2a……ノズル
開口部、3……中間体、4……ポンプシリンダ、
4a……中空孔部、9……真空ブロワ、10……
モータ。
Figures 1 and 2 are drawings related to an embodiment of the present invention, where Figure 1A is a longitudinal sectional front view of the nozzle, and Figure B is Figure A.
20-20 sectional view of Figure C is arrow 21 of Figure A
-21 sectional view, FIG. 2A is a longitudinal sectional front view of the pump cylinder, FIG. B is a plan view of the pump cylinder, and FIG. 3 is a configuration diagram of a known mechanical stirring device. 1... Melting furnace, 2... Nozzle, 2a... Nozzle opening, 3... Intermediate, 4... Pump cylinder,
4a...Hollow hole section, 9...Vacuum blower, 10...
motor.
Claims (1)
に吸込ませ、吐出させる金属溶湯攪拌装置におい
て、上記溶融炉に形成された上記ノズルの開口部
の開口面積は上記ポンプシリンダの下部端面の開
孔部断面積と等しく、且つ該ノズルの開口部は下
部縁が炉床面と同一面にあり、しかも該ノズルの
開口部の形状は上記溶融炉の深さ方向の寸法が横
幅寸法より短く選定されると共に、該ノズルは溶
湯を水平方向に吐出させるに足り且つ炉壁の厚み
より短かい寸法のノズル水平部分と、上記ポンプ
シリンダに連通するノズル傾斜部分とを有するよ
うに構成したことを特徴とする金属溶湯攪拌装置
のノズル構造。 In a molten metal agitation device that causes molten metal in a melting furnace to be sucked into a pump cylinder through a nozzle and then discharged, the opening area of the opening of the nozzle formed in the melting furnace is equal to the cross section of the opening in the lower end face of the pump cylinder. and the lower edge of the opening of the nozzle is on the same plane as the hearth surface, and the shape of the opening of the nozzle is selected so that the dimension in the depth direction of the melting furnace is shorter than the width dimension. , the nozzle is configured to have a horizontal nozzle portion that is sufficient to discharge the molten metal horizontally and is shorter than the thickness of the furnace wall, and an inclined nozzle portion that communicates with the pump cylinder. Nozzle structure of molten metal stirring device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985073146U JPH0413598Y2 (en) | 1985-05-17 | 1985-05-17 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985073146U JPH0413598Y2 (en) | 1985-05-17 | 1985-05-17 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61189198U JPS61189198U (en) | 1986-11-26 |
| JPH0413598Y2 true JPH0413598Y2 (en) | 1992-03-30 |
Family
ID=30612229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1985073146U Expired JPH0413598Y2 (en) | 1985-05-17 | 1985-05-17 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0413598Y2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS597906A (en) * | 1982-07-07 | 1984-01-17 | Mitsubishi Rayon Co Ltd | optical transmission fiber |
| JPS5928834A (en) * | 1982-08-05 | 1984-02-15 | 株式会社日立製作所 | Transformer protecting relay unit |
-
1985
- 1985-05-17 JP JP1985073146U patent/JPH0413598Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61189198U (en) | 1986-11-26 |
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