JPH036436B2 - - Google Patents
Info
- Publication number
- JPH036436B2 JPH036436B2 JP7020084A JP7020084A JPH036436B2 JP H036436 B2 JPH036436 B2 JP H036436B2 JP 7020084 A JP7020084 A JP 7020084A JP 7020084 A JP7020084 A JP 7020084A JP H036436 B2 JPH036436 B2 JP H036436B2
- Authority
- JP
- Japan
- Prior art keywords
- cylinder
- molten metal
- sucked
- water level
- metal
- 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
- 229910052751 metal Inorganic materials 0.000 claims description 36
- 239000002184 metal Substances 0.000 claims description 36
- 238000002844 melting Methods 0.000 claims description 15
- 230000008018 melting Effects 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 229910044991 metal oxide Inorganic materials 0.000 claims description 9
- 150000004706 metal oxides Chemical class 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 11
- 229910052782 aluminium Inorganic materials 0.000 description 9
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】
本発明は金属溶湯撹拌装置における金属酸化物
の洗滌方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning metal oxides in a molten metal stirring apparatus.
アルミニウム、銅、亜鉛などの金属溶融炉で
は、溶湯を撹拌しない場合、溶融時間が長くな
り、しかも加熱すべき温度が高くなるうえ、酸化
物の発生量が多くなるなどの諸欠点が伴ない、低
品質、コスト高の要因となることが知られてい
る。したがつて酸化現象を抑制し高品質の製品を
得るためには、加熱温度を低くし、かつ、溶融に
要する時間を短縮することが要求され、そのため
に上記溶湯を撹拌することが大いに役立つ。アル
ミニウムの場合、撹拌によつて酸化物の発生量、
溶融時間ともに約10%減少することが認められ
る。しかし酸化物の残り90%の発生は除去できな
いのが現状である。 In furnaces for melting metals such as aluminum, copper, and zinc, if the molten metal is not stirred, the melting time becomes longer, the temperature at which it must be heated becomes higher, and the amount of oxides generated increases. It is known to be a cause of low quality and high costs. Therefore, in order to suppress the oxidation phenomenon and obtain a high quality product, it is required to lower the heating temperature and shorten the time required for melting, and stirring the molten metal is very useful for this purpose. In the case of aluminum, the amount of oxide generated by stirring,
Approximately 10% reduction in both melting time was observed. However, the current situation is that the remaining 90% of oxides cannot be removed.
有効な撹拌作業をおこなう機械的撹拌装置の周
知例としては、第1図に示すごとく、溶融炉1の
側壁下部に連通孔2を内設した耐火物による中間
体3を設け、該中間体3に内壁を耐火材料で内張
したポンプシリンダ4を取付ける。上記連通孔2
を介して該ポンプシリンダ4と溶融炉1の内底部
とを連通せしめると共に、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な
どを介在した通気管8により上記ポンプシリンダ
4の上部と真空ブロワ9とを接続せしめる。該真
空ブロワ9はモータ10によつて作動し、前記ポ
ンプシリンダ4内を真空圧力に作動せしめて溶湯
をシリンダ4内に吸引導入し、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に導
入する。真空吸入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、滞留した溶
湯に対流が生じ溶融炉1内は撹拌される。ところ
が金属酸化物12は、
(1) 炉内金属溶湯の表面で酸化が進行するため、
シリンダ4内の溶湯11の表面にも酸化物1
2′が発生し前記シリンダ4内に吸入され吐出
される際、常にシリンダ4内に残留することに
なる。 As a well-known example of a mechanical stirring device that performs an effective stirring operation, as shown in FIG. Attach a pump cylinder 4 whose inner wall is lined with a fireproof material. Above communication hole 2
The pump cylinder 4 is communicated with the inner bottom of the melting furnace 1 through a ventilation pipe 8 which has an automatic switching valve 5 between outside air and negative pressure, a cyclone 6, a filter 7, etc. The upper part of the vacuum blower 9 is connected to the vacuum blower 9. The vacuum blower 9 is operated by a motor 10 to apply vacuum pressure in the pump cylinder 4 to draw the molten metal into the cylinder 4, and after a certain period of time has passed, the automatic switching valve 5 is switched to supply outside air to the cylinder. Introduce. Since the vacuum suction force is removed and outside air is 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 stagnant molten metal and stirring the inside of the melting furnace 1. However, the metal oxide 12 (1) oxidizes on the surface of the molten metal in the furnace;
Oxide 1 is also present on the surface of the molten metal 11 in the cylinder 4.
When 2' is generated, sucked into the cylinder 4, and discharged, it always remains in the cylinder 4.
(2) 冷材を投入する際の操作の不手際によつて溶
湯表面の酸化物12を吸入してしまうことがあ
る。(2) Oxide 12 on the surface of the molten metal may be inhaled due to clumsy operation when charging the refrigerant.
(3) 溶湯11を外部に取り出した結果、炉内の溶
湯水位がシリンダ下部の連通孔2付近まで下が
つた状態でシリンダ4の吸入が行なわれた場
合、表面の金属酸化物12を吸入してしまうこ
とがある。(3) As a result of taking out the molten metal 11, if the molten metal level in the furnace has dropped to near the communication hole 2 at the bottom of the cylinder and the cylinder 4 is inhaled, the metal oxide 12 on the surface will be inhaled. Sometimes it happens.
以上のような理由によつて、シリンダ4内に金
属酸化物が吸入され、しかもいつたん導入された
酸化物はシリンダ4を空にする以外、外に出るこ
とはない。このため酸化物はシリンダ4内の管壁
に付着すると同時に、通常運転で一定吸入される
溶湯の水位14部位に特に金属酸化物の凝着13
が著しく、シリンダ内径を狭めて、作動中シリン
ダ内の溶湯の流れを妨げる結果となる。さらに溶
融炉1は溶湯を外部へ取り出しつつ冷材を投入す
る、いわゆる追い込み操業のため、シリンダ洗滌
がきわめて困難であるなどの欠点があつた。 For the reasons mentioned above, the metal oxide is sucked into the cylinder 4, and once introduced, the oxide does not come out except when the cylinder 4 is emptied. For this reason, oxides adhere to the pipe wall inside the cylinder 4, and at the same time, metal oxides adhere to the water level 14 of the molten metal that is constantly sucked in during normal operation.
This significantly narrows the inner diameter of the cylinder and obstructs the flow of molten metal within the cylinder during operation. Furthermore, since the melting furnace 1 is operated in a so-called run-up operation in which the molten metal is taken out to the outside while the cold material is put in, it has the disadvantage that cleaning the cylinder is extremely difficult.
本発明は以上の問題を解消するためになされた
もので、溶融炉と連通したシリンダ壁内に付着し
た金属酸化物を極めて容易に除去して、高品質の
製品を得るようにする金属溶湯撹拌装置における
酸化物の洗滌方法を提供することを目的とし、溶
融金属を周期的にシリンダ内に、このシリンダを
真空にすることによつて吸こみ、該溶融金属を溶
融炉内に吐出す方式の金属溶湯撹拌装置におい
て、外気と負圧との自動切換バルブに、真空圧の
作動時間長を調節するタイマを取付け、該タイマ
の真空圧作動時間長を長く調整し、かつ吸引され
たシリンダ内の水位を通常時の水位より上昇さ
せ、前記シリンダ内に吸引された通常時の水位付
近のメタル酸化物を自重で落下させることを特徴
とする。 The present invention has been made to solve the above problems, and is a molten metal agitation system that allows metal oxides adhering to the inside of a cylinder wall communicating with a melting furnace to be removed very easily to obtain a high-quality product. The purpose of the present invention is to provide a method for cleaning oxides in an apparatus, in which molten metal is periodically sucked into a cylinder by creating a vacuum in the cylinder, and the molten metal is discharged into a melting furnace. In a molten metal stirring device, a timer that adjusts the operating time of the vacuum pressure is attached to the automatic switching valve between outside air and negative pressure, and the vacuum operating time of the timer is adjusted to a longer time, and the vacuum pressure in the cylinder that is sucked is It is characterized in that the water level is raised above the normal water level, and the metal oxide sucked into the cylinder, which is near the normal water level, falls under its own weight.
次に本発明を図面を参照して説明する。第1図
はアルミニウム金属溶湯撹拌装置の概略的構成図
を示す。金属酸化物は温度を高めることによつ
て、より軟化する性質がある。シリンダ4内に凝
着したアルミニウム酸化物13の温度を高める手
段としては、溶融炉1からシリンダ4への溶融金
属の吸引水位をシリンダの凝着位置を越えたレベ
ルまで高めた溶湯の吸入、排出を繰り返すことに
より行う。この結果、シリンダ4の凝着金属は、
シリンダ4へ吸引された溶融金属の内部に位置す
るので、溶融金属の表面に位置する場合に比べ
て、上記凝着金属の温度が高くなり、シリンダ4
の凝着金属が軟化することになる。さらに、通常
の撹拌時における溶湯温度は、例えば約650℃で
あるが、溶融が完了した後は、700〜750℃に上昇
するから、シリンダ4内の洗滌はこの時期に行う
と、より効果的である。しかし、この時点に限定
されるものではない。他方、モータ10の回転に
より真空ブロワ9を作動させ、シリンダ4内を真
空圧にして、アルミニウム溶湯11をシリンダ4
内に吸引させる。この吸引に際し、予め、外気と
真空ブロワ9との切換時間長を調節するタイマー
を自動切換バルブ5に取付けておく。このタイマ
ー調節によつて通常撹拌時における真空吸入時間
より長い時間の真空吸引後に、自動切換バルブ5
を切換えてシリンダ4に外気を導入させ、シリン
ダ4内に吸入されたアルミニウム溶湯を自重で落
下させて溶融炉1内に吐出させるようにする。即
ち真空吸引時間が長くなつたため、吸入されたア
ルミニウム溶湯のシリンダ4内における水位15
は、通常撹拌時における水位14よりも高くな
る。炉内の溶湯11の高さとの落差がより大きく
なつたことは酸化物の温度上昇による軟化効果と
あいまつて、シリンダ4内に付着したアルミニウ
ム酸化物を効率よく洗滌する。以上説明の金属は
アルミニウムに限らず銅、亜鉛などの場合でもよ
いことは勿論である。本発明は上記洗滌動作を数
回くり返すことにより、いつそう効果的に洗滌を
行ない、高品質の製品を効率的に得る事が出来る
効果を奏する。 Next, the present invention will be explained with reference to the drawings. FIG. 1 shows a schematic diagram of a molten aluminum metal stirring apparatus. Metal oxides have the property of becoming more softened by increasing the temperature. As a means of increasing the temperature of the aluminum oxide 13 that has adhered in the cylinder 4, suction and discharge of the molten metal from the melting furnace 1 into the cylinder 4 is carried out by raising the suction water level of the molten metal to a level exceeding the position of adhesion in the cylinder. This is done by repeating. As a result, the adhered metal in cylinder 4 is
Since it is located inside the molten metal sucked into the cylinder 4, the temperature of the adhered metal becomes higher than when it is located on the surface of the molten metal.
This will cause the adhesive metal to soften. Furthermore, the temperature of the molten metal during normal stirring is, for example, about 650°C, but after the melting is completed, it rises to 700-750°C, so cleaning the inside of the cylinder 4 at this time is more effective. It is. However, it is not limited to this point. On the other hand, the vacuum blower 9 is operated by the rotation of the motor 10 to create a vacuum pressure in the cylinder 4, and the molten aluminum 11 is transferred to the cylinder 4.
Let it be sucked inside. During this suction, a timer for adjusting the switching time length between the outside air and the vacuum blower 9 is attached to the automatic switching valve 5 in advance. With this timer adjustment, after vacuum suction for a longer time than the vacuum suction time during normal stirring, the automatic switching valve 5
is switched to introduce outside air into the cylinder 4, and the molten aluminum sucked into the cylinder 4 is caused to fall under its own weight and discharged into the melting furnace 1. That is, since the vacuum suction time became longer, the water level of the sucked molten aluminum in the cylinder 4 decreased by 15.
is higher than the water level 14 during normal stirring. The larger height difference between the height of the molten metal 11 in the furnace and the softening effect of the oxide due to the temperature rise makes it possible to efficiently wash away the aluminum oxide adhering to the inside of the cylinder 4. It goes without saying that the metal described above is not limited to aluminum, but may also be copper, zinc, or the like. According to the present invention, by repeating the above-mentioned washing operation several times, the washing can be carried out more effectively and a high-quality product can be efficiently obtained.
第1図は従来のアルミニウム金属溶湯撹拌装置
の概略的構成を示す。
1……金属溶融炉、2……連通孔、3……中間
体、4……シリンダ、5……自動切換バルブ、6
……サイクロン、7……フイルター、8……通気
管、9……真空ブロワー、10……可変速モータ
ー、11……アルミニウム溶湯、12……アルミ
ニウム酸化物、12′……シリンダ内部のアルミ
ニウム酸化物、13……シリンダ内壁に凝着した
アルミニウム酸化物、14……通常撹拌時の吸入
アルミニウム溶湯の水位、15……洗滌時の吸入
アルミニウム溶湯の水位。
FIG. 1 shows a schematic configuration of a conventional aluminum metal molten metal stirring device. DESCRIPTION OF SYMBOLS 1...Metal melting furnace, 2...Communication hole, 3...Intermediate body, 4...Cylinder, 5...Automatic switching valve, 6
... Cyclone, 7 ... Filter, 8 ... Ventilation pipe, 9 ... Vacuum blower, 10 ... Variable speed motor, 11 ... Aluminum molten metal, 12 ... Aluminum oxide, 12' ... Aluminum oxide inside the cylinder 13...Aluminum oxide adhered to the cylinder inner wall, 14...Water level of sucked molten aluminum during normal stirring, 15...Water level of sucked molten aluminum during cleaning.
Claims (1)
に該シリンダを真空にして吸こみ、該溶融金属を
上記炉内に吐き出す方式の金属溶湯撹拌装置にお
いて、前記シリンダへの真空圧と外気とを切換え
る自動切換バルブに、真空圧の作動時間長を調節
するタイマーを取付け、該タイマの真空圧作動時
間長を長く調節し、かつ吸引されたシリンダ内の
水位を通常時の水位より上昇させ、前記シリンダ
内に吸引された通常時の水位付近のメタル酸化物
を自重で落下させることを特徴とする金属溶湯撹
拌装置における酸化物の洗滌方法。1. In a molten metal stirring device of a type in which molten metal in a melting furnace is periodically sucked into a cylinder by evacuating the cylinder and the molten metal is discharged into the furnace, the vacuum pressure to the cylinder and the outside air are Attaching a timer for adjusting the operating time of the vacuum pressure to the automatic switching valve that switches the valve, adjusting the vacuum operating time of the timer to a longer time, and raising the water level in the sucked cylinder above the normal water level, A method for cleaning oxides in a molten metal stirring device, characterized in that the metal oxides near the normal water level sucked into the cylinder are allowed to fall under their own weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7020084A JPS60213789A (en) | 1984-04-09 | 1984-04-09 | Method of washing oxide in molten metal agitator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7020084A JPS60213789A (en) | 1984-04-09 | 1984-04-09 | Method of washing oxide in molten metal agitator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60213789A JPS60213789A (en) | 1985-10-26 |
| JPH036436B2 true JPH036436B2 (en) | 1991-01-30 |
Family
ID=13424631
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7020084A Granted JPS60213789A (en) | 1984-04-09 | 1984-04-09 | Method of washing oxide in molten metal agitator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60213789A (en) |
-
1984
- 1984-04-09 JP JP7020084A patent/JPS60213789A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60213789A (en) | 1985-10-26 |
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