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JPH0343227Y2 - - Google Patents

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Publication number
JPH0343227Y2
JPH0343227Y2 JP5327985U JP5327985U JPH0343227Y2 JP H0343227 Y2 JPH0343227 Y2 JP H0343227Y2 JP 5327985 U JP5327985 U JP 5327985U JP 5327985 U JP5327985 U JP 5327985U JP H0343227 Y2 JPH0343227 Y2 JP H0343227Y2
Authority
JP
Japan
Prior art keywords
gas supply
inert gas
molten metal
melting
holding chamber
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
Application number
JP5327985U
Other languages
Japanese (ja)
Other versions
JPS61185992U (en
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Filing date
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Priority to JP5327985U priority Critical patent/JPH0343227Y2/ja
Publication of JPS61185992U publication Critical patent/JPS61185992U/ja
Application granted granted Critical
Publication of JPH0343227Y2 publication Critical patent/JPH0343227Y2/ja
Expired legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Treatment Of Steel In Its Molten State (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、アルミニウム合金やマグネシウム合
金等の軽金属を溶解するための軽合金溶解炉に関
し、更に詳しくは、砂型鋳物、金型鋳物、ダイカ
ストその他の鋳物製品を鋳造するため、水素ガス
含有量の少ない溶湯を供給するのに供される軽合
金溶解炉に関するものである。
[Detailed description of the invention] [Industrial application field] The present invention relates to a light alloy melting furnace for melting light metals such as aluminum alloys and magnesium alloys. This invention relates to a light alloy melting furnace that is used to supply molten metal with a low hydrogen gas content in order to cast cast products.

〔従来技術〕[Prior art]

この種の軽合金溶解炉は、重油バーナまたはガ
スバーナによる輻射熱を利用して軽合金材料を溶
解する反射炉が、従来より主として採用されてい
る。この反射炉では、溶解炉の内部において脱ガ
ス精錬を行わず、フラツクスを使用した除滓処理
のみ行つているのが通例である。そして、水素ガ
ス含有量が少なく清浄度の高い良質の溶湯を得る
ために必要不可欠とされる脱ガス精錬処理につい
ては、反射炉に連設された前炉または保持炉にて
行う用に構成されており、前記反射炉から移送さ
れて来た溶湯を前炉または保持炉で脱ガス精錬を
行い、その後、鋳型や鋳造機等へ給湯するもので
あつた。
Conventionally, this type of light alloy melting furnace has mainly been a reverberatory furnace that melts light alloy materials using radiant heat from a heavy oil burner or a gas burner. In this reverberatory furnace, it is customary to perform no degassing and refining inside the melting furnace, but only a sludge removal process using flux. The degassing refining process, which is essential for obtaining high-quality molten metal with low hydrogen gas content and high purity, is configured to be carried out in a forehearth or holding furnace connected to a reverberatory furnace. The molten metal transferred from the reverberatory furnace was degassed and refined in a forehearth or holding furnace, and then fed to molds, casting machines, etc.

また近年には、第5図に示したように、材料の
加熱に輻射熱を利用せず、溶解室30に装入され
た材料Aをバーナ31による直火で加熱して溶解
時間を短縮すると共に、溶解室30への材料装入
部を煙道と兼用させて、排ガスによる材料Aの予
熱を行うようにした省エネルギー型の溶解炉32
が一般に採用されるに至つている。この種の溶解
炉32においても、溶解速度は速いものの湯量調
節および精錬が困難であることに起因して、溶解
炉32とは別に前炉33や図示しない保持炉を具
備しているのが実情である。
In addition, in recent years, as shown in FIG. 5, instead of using radiant heat to heat the material, the material A charged into the melting chamber 30 is heated with direct flame by the burner 31 to shorten the melting time. , an energy-saving melting furnace 32 in which the material charging part into the melting chamber 30 is also used as a flue, and material A is preheated by exhaust gas.
has come to be generally adopted. Even in this type of melting furnace 32, although the melting speed is fast, it is difficult to adjust the amount of hot metal and refine it, so the fact is that it is equipped with a forehearth 33 and a holding furnace (not shown) in addition to the melting furnace 32. It is.

アルミニウム合金を精錬する場合、通常は次の
手順により行われている。
When refining aluminum alloys, the following procedure is usually used.

(1) 脱滓処理 この処理は溶解炉32の保持室34内部で行わ
れる。材料の溶け落ち後、比較的低温の700℃前
後でNac,Kc,NaF等の塩基性フラツクス
を溶湯の1%程度添加し、溶湯Bを攪拌しながら
精錬し、浮上した滓を除去することによつて行わ
れる。
(1) De-slag treatment This treatment is performed inside the holding chamber 34 of the melting furnace 32. After the material has melted down, basic fluxes such as Nac, Kc, NaF, etc. are added to the molten metal at a relatively low temperature of around 700°C, and about 1% of the molten metal is added, and the molten metal B is refined while stirring, and the floating slag is removed. It is done by folding.

(2) 脱ガス処理 この脱ガス処理は、前炉33若しくは図示しな
い保持炉で行われるのが通例であり、その処理方
法を大別すれば、 ヘキサクロロエタンを含む脱ガスフラツク
スの添加による処理 塩素ガスの吹き込みによる処理 窒素ガスの吹き込みによる処理 等がある。大型溶解炉ではランスを用いて上記
またはの方法で処理することが多い。上記お
よびの処理方法は、脱ガス効果は大きいもの
の、人体に有毒な塩素ガスを発生するので公害防
止の観点から望ましくない、現に用いられなくな
りつつある。また上記の処理方法は、機械的に
溶湯中の水素ガスを窒素ガスの気泡に吸着させて
脱ガスする方法であるため、溶湯中にいかに多く
の気泡をより微細に分散させるかが重要である。
(2) Degassing treatment This degassing treatment is usually carried out in the forehearth 33 or a holding furnace (not shown), and the treatment methods can be roughly divided into: treatment by adding a degassing flux containing hexachloroethane, treatment by adding a degassing flux containing hexachloroethane, chlorine gas Treatment by blowing in nitrogen gas. Treatment by blowing in nitrogen gas, etc. In large melting furnaces, lances are often used for processing using the above method or the method described above. Although the above treatment methods have a large degassing effect, they generate chlorine gas that is toxic to the human body, and are therefore undesirable from the viewpoint of pollution prevention, and are currently no longer being used. Furthermore, since the above treatment method is a method of mechanically degassing hydrogen gas in the molten metal by adsorbing it to nitrogen gas bubbles, it is important to disperse as many bubbles as possible into the molten metal in a finer manner. .

〔考案の目的〕[Purpose of invention]

本考案は、上記従来の問題点を考慮してなされ
たものであつて、溶解後、脱滓処理はもとより脱
ガス処理についも溶解炉の保持室で行い得るよう
に構成して従来の前炉や保持炉をなくし、これに
より溶解炉から鋳型もしくは鋳造機への直接給湯
を可能にすると共に、脱ガス効果についても十分
に奏し得る軽合金溶解炉の提供を目的とするもの
である。
The present invention has been made in consideration of the above-mentioned conventional problems, and is configured so that after melting, not only the de-slag treatment but also the degassing treatment can be performed in the holding chamber of the melting furnace, unlike the conventional forefurnace. The object of the present invention is to provide a light alloy melting furnace which eliminates the need for a holding furnace and enables direct supply of hot water from the melting furnace to a mold or casting machine, and which also has a sufficient degassing effect.

〔考案の構成〕[Structure of the idea]

本考案の軽合金溶解炉は、上記の目的を達成する
ために、溶解室に連通して、炉底部に湯溜部を有
する保持室が形成された溶解炉において、前記保
持室の天井部に不活性ガス供給源に接続された不
活性ガス供給装置が装着され、この不活性供給装
置の下端の不活性ガス供給部が前記保持室内の溶
湯中に浸漬可能となるように昇降自在に設けられ
るとともに、該不活性ガス供給部におけるガス供
給路の送端部に、前記湯溜部内の溶湯に接しうる
多孔質プラグが設けられており、これにより前記
保持室内で脱滓処理および脱ガス処理の精錬を行
えるように構成したことを特徴とするものであ
る。
In order to achieve the above object, the light alloy melting furnace of the present invention is a melting furnace in which a holding chamber is formed in communication with the melting chamber and has a sump at the bottom of the furnace. An inert gas supply device connected to an inert gas supply source is installed, and the inert gas supply section at the lower end of the inert gas supply device is provided so as to be movable up and down so that it can be immersed in the molten metal in the holding chamber. At the same time, a porous plug that can come into contact with the molten metal in the sump is provided at the sending end of the gas supply path in the inert gas supply section, so that descaling and degassing can be carried out in the holding chamber. It is characterized by being configured so that it can be refined.

〔実施例〕〔Example〕

本考案の一実施例を第1図乃至第4図に基づい
て説明すれば、以下の通りである。
An embodiment of the present invention will be described below with reference to FIGS. 1 to 4.

溶解炉1には、その内部に、材料装入口2側に
形成された溶解室3と、該溶解室3に連通され、
出湯口4側に形成された保持室5とが備えられて
いる。この溶解室3には溶解室バーナ6が、また
保持室5には保持室バーナ7がそれぞれもうけら
れる一方、保持室5の炉底部には湯溜部8が形成
されている。
The melting furnace 1 includes a melting chamber 3 formed inside thereof on the side of the material charging port 2, and a melting chamber 3 communicating with the melting chamber 3,
A holding chamber 5 formed on the outlet 4 side is provided. A melting chamber burner 6 is provided in the melting chamber 3, a holding chamber burner 7 is provided in the holding chamber 5, and a sump 8 is formed at the bottom of the holding chamber 5.

前記溶解室3に形成されて材料装入口2は煙道9
と接続可能に設けられていて、保持室5等から発
生した排熱は溶解室3を通じて煙道9に導かれ、
これによつて溶解室3内の装入された材料を予熱
しうるように構成されている。
The material charging port 2 formed in the melting chamber 3 is connected to a flue 9.
The exhaust heat generated from the holding chamber 5 etc. is guided to the flue 9 through the melting chamber 3,
This allows the material charged in the melting chamber 3 to be preheated.

一方、前記保持室5の天井部には、不活性ガス
供給装置10が装着されている。この不活性ガス
供給装置10は第4図に示したように、窒素ガス
等の不活性ガス供給源に接続された不活性ガス導
入パイプ11と、該導入パイプ11の下端に連結
され耐熱性かつ可浸漬性をゆうする不活性ガス供
給部12とを備えている。前記導入パイプ11及
び供給部12は、その内部にガス供給路13が連
通して形成され、前記供給部12側に形成された
ガス供給路13の送端部には、湯溜部8内の溶湯
Bと接面しうるように多孔質プラグ14が埋設さ
れている。上記の不活性ガス供給装置10は保持
室5の天井部に装着され、常時は前記不活性ガス
供給部12が保持室5の上方に待機し、脱ガス処
理時において不活性ガス供給部12が降下して保
持室5内の溶湯B中に浸漬可能となるように昇降
自在に構成されている。
On the other hand, an inert gas supply device 10 is mounted on the ceiling of the holding chamber 5. As shown in FIG. 4, this inert gas supply device 10 includes an inert gas introduction pipe 11 connected to an inert gas supply source such as nitrogen gas, and a heat-resistant and It is equipped with an inert gas supply section 12 that is immersable. The introduction pipe 11 and the supply part 12 are formed with a gas supply passage 13 communicating therein, and the gas supply passage 13 formed on the supply part 12 side has a gas supply passage 13 at the feeding end of the gas supply passage 13 in the tundish part 8. A porous plug 14 is buried so as to be in contact with the molten metal B. The inert gas supply device 10 described above is mounted on the ceiling of the holding chamber 5, and the inert gas supply section 12 is normally on standby above the holding chamber 5, and the inert gas supply section 12 is turned on during degassing processing. It is configured to be movable up and down so that it can be lowered and immersed in the molten metal B in the holding chamber 5.

また上記の溶解炉1は、シリンダ15により傾
動可能に設けられる一方、同溶解炉1の出湯口4
に隣接してトイ予熱用バーナ21及びトイ保温カ
バー22を備えた旋回式湯路16が設置され、該
旋回式湯路16の送湯端下方には、砂型鋳物機1
7の受湯口18が3箇所い形成されている。
Further, the melting furnace 1 described above is provided so as to be tiltable by the cylinder 15, while the melting furnace 1 has a tap opening 4.
A rotating waterway 16 equipped with a toy preheating burner 21 and a toy heat-insulating cover 22 is installed adjacent to the toy preheating burner 21 and a toy heat-insulating cover 22 .
Three receiving ports 18 of No. 7 are formed.

上記の構成において、本考案の軽合金溶解炉を
使用して溶解・鋳造する手順は次の通りである。
In the above configuration, the procedure for melting and casting using the light alloy melting furnace of the present invention is as follows.

先ずトツプバケツト19に、アルミニウム合金
等の軽合金材料であるインゴツト及び返り材を収
容し、電動横行機構を備えたホイスト20を駆動
させて、溶解炉1の材料装入口2から溶解室3内
に材料を装入する、この時点では、保持室5に設
けられた不活性ガス供給部12は保持室5の天井
側近傍の上昇端に待機されている。
First, ingots and return material made of light alloy materials such as aluminum alloy are placed in the top bucket 19, and the hoist 20 equipped with an electric traverse mechanism is driven to transport the materials from the material charging port 2 of the melting furnace 1 into the melting chamber 3. At this point in time when the holding chamber 5 is charged, the inert gas supply section 12 provided in the holding chamber 5 is on standby at the rising end near the ceiling side of the holding chamber 5.

次に、溶解室バーナ6による加熱によつて溶解
室3の材料が溶け落ちて溶解されると、全ての溶
解室バーナ6および保持室バーナ7を停止して、
約700℃の溶湯温度下でフラツクス精錬による脱
滓処理を行う、この脱滓処理は、先述した従来例
と同様の方法によつて行われる。
Next, when the material in the melting chamber 3 is melted down and melted by heating by the melting chamber burner 6, all the melting chamber burners 6 and holding chamber burners 7 are stopped.
The slag removal process is performed by flux refining at a molten metal temperature of approximately 700°C, and is performed in the same manner as in the conventional example described above.

脱滓処理が終了すると、保持室バーナ7に着火
して、保持室5の湯溜部8に集溜されている溶湯
Bを約750〜760℃まで昇温させる。その後、保持
室バーナ7を停止し、不活性ガス供給装置10の
供給部12を保持室5の炉床まで降下させて、溶
湯B中に浸漬する。このときの多孔質プラグ14
の上面から溶湯表面までの浸漬深さはh、450mm
以上に設定することが望ましい。尚、この種の軽
合金溶解炉においては、通常、溶湯の深さが400
〜450mmとなるように構成されているが、本考案
では不活性ガス供給装置10の浸漬量を考慮し
て、溶湯の深さHが550〜600mm以上となるように
保持室5の湯溜部8の深さを設定することが好ま
しい。溶湯の深さHが大きくなると、例えば600
mmの深さで溶湯上部はその下部より20〜30℃程度
高温になるといつた温度分布のアンバランスを生
じるが、これは後述する窒素ガスのバブリングに
より溶湯が攪拌されるで、溶湯の温度分布は均一
化される。
When the slag removal process is completed, the holding chamber burner 7 is ignited to raise the temperature of the molten metal B collected in the sump 8 of the holding chamber 5 to approximately 750 to 760°C. Thereafter, the holding chamber burner 7 is stopped, and the supply section 12 of the inert gas supply device 10 is lowered to the hearth of the holding chamber 5, and immersed in the molten metal B. Porous plug 14 at this time
The immersion depth from the top surface to the molten metal surface is h, 450mm.
It is desirable to set the value above. In addition, in this type of light alloy melting furnace, the depth of the molten metal is usually 400 mm.
However, in the present invention, considering the amount of immersion of the inert gas supply device 10, the depth H of the holding chamber 5 is adjusted so that the depth H of the molten metal is 550 to 600 mm or more. It is preferable to set the depth to 8. As the depth H of the molten metal increases, for example, 600
mm depth, the upper part of the molten metal becomes about 20 to 30°C hotter than the lower part, causing an imbalance in the temperature distribution.This is because the molten metal is stirred by nitrogen gas bubbling, which will be described later. is equalized.

不活性ガス供給装置10の供給部12を溶湯B
中に浸漬して炉床の所定位置に設定した後、不活
性ガス導入パイプ11を通じて窒素ガスを吹き込
む。この窒素ガスは、ガス供給路13により多孔
質プラグ14へと導かれ、該多孔質プラグ14か
らは窒素ガスの無数の微細な気泡が発生する。こ
の気泡により溶湯Bが攪拌されるので、溶湯Bの
温度分布が均一になる。また、多孔質プラグ14
から発生した気泡は、溶湯Bの表面に到達するま
での間に溶湯B中の水素ガスを吸着するので、こ
れによつて脱ガス処理が行われる。かかる脱ガス
処理を約20分間行うことにより、溶湯B中の水素
ガス含有量は0.12c.c./100g程度まで減少し、水素
ガス含有量の少ない清浄な溶湯が得られる。
The supply section 12 of the inert gas supply device 10 is connected to the molten metal B.
After being immersed in the liquid and set at a predetermined position on the hearth, nitrogen gas is blown through the inert gas introduction pipe 11. This nitrogen gas is guided to the porous plug 14 by the gas supply path 13, and countless fine bubbles of nitrogen gas are generated from the porous plug 14. Since the bubbles stir the molten metal B, the temperature distribution of the molten metal B becomes uniform. In addition, the porous plug 14
The bubbles generated from the molten metal B adsorb hydrogen gas in the molten metal B before reaching the surface of the molten metal B, thereby performing a degassing process. By performing this degassing treatment for about 20 minutes, the hydrogen gas content in the molten metal B is reduced to about 0.12 cc/100g, and a clean molten metal with a low hydrogen gas content is obtained.

脱ガス処理終了後、溶湯Bの表面に浮遊せる残
滓を除去する一方、前記不活性ガス供給部12を
元の待機位置まで上昇させる。これにより多孔質
プラグ14は目詰まりを回避され、かつメンテナ
ンスが容易となる、しかる後、シリンダ15によ
り炉体を所定の傾斜角度まで傾動させ、出湯口4
から旋回式湯路16へ出湯する。この溶湯は旋回
式湯路16の上流端から下流端へと流れ、砂型鋳
造機17の上部に設定され湯溜りとなる各受湯口
18に供給され、図示しないストツパーを引き抜
くことにより鋳型内のキヤビテイに注湯されるも
のである。
After the degassing process is completed, the residue floating on the surface of the molten metal B is removed, while the inert gas supply section 12 is raised to its original standby position. This prevents the porous plug 14 from clogging and facilitates maintenance. After that, the cylinder 15 tilts the furnace body to a predetermined angle of inclination, and the outlet 4
From there, the hot water is discharged to the swirling hot water path 16. This molten metal flows from the upstream end to the downstream end of the swirling channel 16, and is supplied to each inlet 18 that is set at the top of the sand casting machine 17 and serves as a sump.By pulling out a stopper (not shown), the mold cavity is closed. Hot water is poured into the water.

〔考案の効果〕[Effect of idea]

本考案に係る軽合金溶解炉は以上のように、溶
解室に連通して、炉底部に湯溜部を有する保持室
が形成された溶解炉において、前記保持室の天井
部に、不活性ガス供給源に接続された不活性ガス
供給装置が装着され、この不活性ガス供給装置の
下端の不活性ガス供給部が前記保持室内の溶湯中
に浸漬可能となるように昇降自在に設けられると
ともに、該不活性ガス供給部におけるガス供給路
の送端部に、前記湯溜部内の溶湯に接しうる多孔
質プラグが設けられた構成であるから、溶解炉内
での脱ガス精錬が可能となる。その結果、従来よ
り必要とされていた前炉や保持炉は不要となり、
これによつて製造コストの大幅な低減、小型化、
設置スペースの縮小などを実現すると共に、溶解
炉から鋳型または鋳造機への直接給湯が可能とな
る。また多孔質プラグが溶湯中に深く浸漬してこ
の多孔質プラグから微細な不活性ガスの気泡を発
生するので、溶湯中の水素ガスを効率良く吸着さ
せて脱ガス処理することが出来る等の優れた諸効
果を奏する。
As described above, the light alloy melting furnace according to the present invention is a melting furnace in which a holding chamber is formed that communicates with the melting chamber and has a sump at the bottom of the furnace, and an inert gas is provided in the ceiling of the holding chamber. An inert gas supply device connected to a supply source is installed, and the inert gas supply section at the lower end of the inert gas supply device is provided to be movable up and down so that it can be immersed in the molten metal in the holding chamber, Since the inert gas supply section has a structure in which a porous plug that can come into contact with the molten metal in the sump section is provided at the sending end of the gas supply path, degassing refining within the melting furnace becomes possible. As a result, the forehearth and holding furnace that were previously required are no longer necessary.
This significantly reduces manufacturing costs, downsizes the
In addition to reducing the installation space, it also becomes possible to supply hot water directly from the melting furnace to the mold or casting machine. In addition, since the porous plug is deeply immersed in the molten metal and generates fine inert gas bubbles, hydrogen gas in the molten metal can be efficiently adsorbed and degassed. It produces various effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案の一実施例を示す要部縦断側面
図、第2図はその要部縦断正面図、第3図は同平
面図、第4図は本考案の構成部をなす不活性ガス
供給装置の要部縦断した使用状態説明図、第5図
は従来例の縦断面図である。 1は溶解炉、2は材料装入口、3は溶解室、5
は保持室、6は溶解室バーナ、7は保持室バー
ナ、8は湯溜部、9は煙道、10は不活性ガス供
給装置、11は不活性ガス導入パイプ、12は不
活性ガス供給部、13はガス供給路、14は多孔
質プラグである。
Fig. 1 is a longitudinal sectional side view of the main part showing an embodiment of the present invention, Fig. 2 is a longitudinal sectional front view of the main part, Fig. 3 is a plan view of the same, and Fig. 4 is an inert material forming a component of the invention. FIG. 5 is a longitudinal cross-sectional view of a conventional example, which is an explanatory diagram of the usage state in which the main part of the gas supply device is longitudinally cut. 1 is a melting furnace, 2 is a material charging port, 3 is a melting chamber, 5
1 is a holding chamber, 6 is a melting chamber burner, 7 is a holding chamber burner, 8 is a water reservoir, 9 is a flue, 10 is an inert gas supply device, 11 is an inert gas introduction pipe, 12 is an inert gas supply section , 13 is a gas supply path, and 14 is a porous plug.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 溶解室に連通して、炉底部に湯溜部を有する保
持室が形成された溶解炉において、前記保持室の
天井部に、不活性ガス供給源に接続された不活性
ガス供給装置が装着され、この不活性ガス供給装
置の下端の不活性ガス供給部が前記保持室内の溶
湯中に浸漬可能となるように昇降自在に設けられ
るとともに、該不活性ガス供給部におけるガス供
給路の送端部に、前記湯溜部内の溶湯に接しうる
多孔質プラグが設けられていることを特徴とする
軽合金溶解炉。
In a melting furnace in which a holding chamber is formed that communicates with the melting chamber and has a sump at the bottom of the furnace, an inert gas supply device connected to an inert gas supply source is attached to the ceiling of the holding chamber. , the inert gas supply section at the lower end of the inert gas supply device is provided so as to be movable up and down so as to be immersed in the molten metal in the holding chamber, and the sending end of the gas supply path in the inert gas supply section A light alloy melting furnace characterized in that a porous plug is provided that can come into contact with the molten metal in the sump.
JP5327985U 1985-04-10 1985-04-10 Expired JPH0343227Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5327985U JPH0343227Y2 (en) 1985-04-10 1985-04-10

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5327985U JPH0343227Y2 (en) 1985-04-10 1985-04-10

Publications (2)

Publication Number Publication Date
JPS61185992U JPS61185992U (en) 1986-11-20
JPH0343227Y2 true JPH0343227Y2 (en) 1991-09-10

Family

ID=30573987

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5327985U Expired JPH0343227Y2 (en) 1985-04-10 1985-04-10

Country Status (1)

Country Link
JP (1) JPH0343227Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016011792A (en) * 2014-06-30 2016-01-21 株式会社広築 Melting and holding furnace of non-ferrous metal and method for replacement and repair of refractory of melting furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016011792A (en) * 2014-06-30 2016-01-21 株式会社広築 Melting and holding furnace of non-ferrous metal and method for replacement and repair of refractory of melting furnace

Also Published As

Publication number Publication date
JPS61185992U (en) 1986-11-20

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