JPH06299263A - Method for removing slag from al or al alloy molten metal - Google Patents
Method for removing slag from al or al alloy molten metalInfo
- Publication number
- JPH06299263A JPH06299263A JP8484093A JP8484093A JPH06299263A JP H06299263 A JPH06299263 A JP H06299263A JP 8484093 A JP8484093 A JP 8484093A JP 8484093 A JP8484093 A JP 8484093A JP H06299263 A JPH06299263 A JP H06299263A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- molten metal
- oxide
- alloy
- 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.)
- Withdrawn
Links
- 239000002893 slag Substances 0.000 title claims abstract description 72
- 239000002184 metal Substances 0.000 title claims abstract description 49
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 49
- 229910000838 Al alloy Inorganic materials 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 13
- 238000002844 melting Methods 0.000 claims abstract description 12
- 230000008018 melting Effects 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 7
- 239000003832 thermite Substances 0.000 claims description 16
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 9
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 4
- 230000009467 reduction Effects 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 4
- 229910052681 coesite Inorganic materials 0.000 abstract 2
- 229910052906 cristobalite Inorganic materials 0.000 abstract 2
- 239000000377 silicon dioxide Substances 0.000 abstract 2
- 235000012239 silicon dioxide Nutrition 0.000 abstract 2
- 229910052682 stishovite Inorganic materials 0.000 abstract 2
- 229910052905 tridymite Inorganic materials 0.000 abstract 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 8
- 239000010410 layer Substances 0.000 description 7
- 238000007670 refining Methods 0.000 description 7
- 229910052736 halogen Inorganic materials 0.000 description 5
- 150000002367 halogens Chemical class 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 229910045601 alloy Inorganic materials 0.000 description 4
- 239000000956 alloy Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 229910052755 nonmetal Inorganic materials 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910016569 AlF 3 Inorganic materials 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- DZGCGKFAPXFTNM-UHFFFAOYSA-N ethanol;hydron;chloride Chemical compound Cl.CCO DZGCGKFAPXFTNM-UHFFFAOYSA-N 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 150000002366 halogen compounds Chemical class 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000039 hydrogen halide Inorganic materials 0.000 description 1
- 239000012433 hydrogen halide Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000005482 strain hardening Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、AlまたはAl合金
(以下、Al合金で代表する)を溶製するに当たり、湯
面に浮上する滓を効率よく除去する方法に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for efficiently removing slag floating on a molten metal surface when smelting Al or an Al alloy (hereinafter represented by an Al alloy).
【0002】[0002]
【従来の技術】Al合金は鉄鋼材料に比べて軽量で比強
度が高く且つ耐食性においても優れたものであることか
ら、自動車や電車等の車輌用外板材や部品材料、建築材
料、家庭用電気製品の外板材、缶材等として幅広く利用
されている。これらAl合金製品を得るまでの製造工程
を略示すると次の通りである。2. Description of the Related Art Since Al alloys are lighter in weight, have higher specific strength and are more excellent in corrosion resistance than steel materials, they are used as outer panel materials and parts materials for vehicles such as automobiles and trains, building materials, and household electrical appliances. It is widely used as an outer plate material and can material for products. The manufacturing process for obtaining these Al alloy products is as follows.
【0003】溶製原料(地金やスクラップ等)→溶解・
精錬→除滓→鋳造→ソーキング→熱間加工→冷間加工→
熱処理→表面処理→検査→出荷 ここで溶解・精錬工程では、溶製原料表面の酸化物(ア
ルマイト等)や溶解・精錬工程で生成する酸化物等が滓
として湯面に浮上してくる。この滓は酸化物を主体とす
る非金属成分とメタル分(Al合金)が混在したもので
あり、この滓をそのまま放置しておくと非金属成分がA
l合金溶湯内へ混入して溶湯汚染を生じるばかりでな
く、出湯後の炉壁や炉底部に付着堆積して溶解炉の容積
を減少せしめ、生産性にも悪影響を及ぼしてくる。Melting raw materials (metals, scraps, etc.) → melting
Refining → Slag → Casting → Soaking → Hot working → Cold working →
Heat treatment → Surface treatment → Inspection → Shipping Here, in the melting / refining process, oxides (alumite, etc.) on the surface of the smelting raw material and oxides generated in the melting / refining process float on the surface of the molten metal as slag. This slag is a mixture of a non-metal component mainly composed of oxide and a metal component (Al alloy). If the slag is left as it is, the non-metal component is A
Not only does it mix into the molten alloy but cause contamination of the molten alloy, but it also adheres and deposits on the furnace wall and furnace bottom after tapping, which reduces the volume of the melting furnace and adversely affects the productivity.
【0004】そこで溶解・精錬後は早期に湯面からの除
滓を行なうことが必要となる。しかしこの滓は上記の様
に多量のメタル分を包含していて溶湯との親和性が高い
ため湯離れが悪く、そのまま強引に湯面上から除滓しよ
うとすると多量のメタル分を伴って排出されることにな
るため、Al合金溶湯の歩留りを著しく低下させる。そ
こで除滓性を高めるための手段として現在汎用されてい
るのは、たとえばKCl−AlF3 等の様な塩化物や沸
化物を主体とするフラックスを散布し、あるいはハロゲ
ン系ガス(Cl2 、六塩化エタン、フロン等)を滓中に
吹込み、滓中のメタル分の一部を着火・燃焼させること
によって滓層全体を昇温せしめ、固体状態で混在してい
るメタル分を溶解して溶湯へ戻すと共に、酸化物等はよ
り安定で且つ溶湯との濡れ性の悪い酸化物に変化させ、
湯離れを良くしてから除滓する方法が採用されている。Therefore, it is necessary to remove slag from the surface of the molten metal as soon as possible after melting and refining. However, since this slag contains a large amount of metal as described above and has a high affinity with the molten metal, it is difficult to separate the molten metal, and if it is forcibly attempted to remove it from the surface of the molten metal, it will be discharged with a large amount of metal. Therefore, the yield of the molten Al alloy is significantly reduced. Therefore what is currently widely used as means for increasing the skimming properties, for example, KCl-AlF 3 chloride or boiling products such as such as sparging with flux mainly or halogen-based gas (Cl 2,, six (Ethanol chloride, Freon, etc.) is blown into the slag, and the entire slag layer is heated by igniting and burning part of the metal components in the slag, melting the metal components mixed in the solid state At the same time, the oxides are changed to more stable and poor wettability with the molten metal.
The method of removing the slag after improving the hot water separation is adopted.
【0005】しかしながらこの除滓工程で使用する精錬
剤はハロゲン系であり、高温の処理条件下で有害なハロ
ゲンガスやハロゲン化水素ガスが多量生成するため、作
業環境を著しく汚染して健康障害の要因となる。However, the refining agent used in this slag removal process is a halogen type, and a large amount of harmful halogen gas and hydrogen halide gas are produced under high-temperature processing conditions, so that the working environment is significantly polluted to cause a health hazard. It becomes a factor.
【0006】[0006]
【発明が解決しようとする課題】本発明は上記の様な事
情に着目してなされたものであって、その目的は、Al
合金原料の溶解・精錬工程で生成する滓を、有害なハロ
ゲン系精錬剤を使用することなく湯面上から効率良く除
去することのできる方法を提供しようとするものであ
る。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and its purpose is to
An object of the present invention is to provide a method capable of efficiently removing slag generated in the melting / refining process of alloy raw materials from the surface of a molten metal without using a harmful halogen-based refining agent.
【0007】[0007]
【課題を解決するための手段】上記課題を解決すること
のできた本発明に係る除滓法の構成は、AlまたはAl
合金を溶解するに当たり、AlまたはAl合金溶湯表面
の滓に、Alとテルミット反応を生ずる酸化物を添加
し、滓中に含まれるAlと該酸化物との反応により滓を
加熱してから除滓するところに要旨を有するものであ
る。ここで使用される酸化物としてはSiO2 ,Fe2
O3 ,W2 O5 ,Mo2 O5 等が例示されるが、除滓性
向上効果やコスト等を総合的に考えて最も好ましいのは
SiO2 もしくはこれと酸化鉄との混合物である。The constitution of the slag removal method according to the present invention which has been able to solve the above-mentioned problems is Al or Al.
In melting the alloy, an oxide that causes a thermite reaction with Al is added to the slag on the surface of Al or the molten Al alloy, and the slag is heated after the slag is heated by the reaction between Al contained in the slag and the oxide. The point is where you do. The oxide used here is SiO 2 , Fe 2
O 3 , W 2 O 5 , Mo 2 O 5 and the like are exemplified, but SiO 2 or a mixture thereof with iron oxide is most preferable in view of the effect of improving the slag removal property and the cost.
【0008】[0008]
【作用】本発明では、前述の如く滓を昇温させてメタル
分を溶解し且つ酸化物をより湯離れの良い酸化物に変え
るための加熱源として、Alとテルミット反応を生ずる
酸化物(以下、テルミット反応性酸化物)を使用する。
即ちテルミット反応とは、下記式で示される如く、Al
による酸化物の高温還元反応を通称するものであり、 2nAl+3MOn →nAl2 O3 +3M+Q 式中、Mは酸化物を形成する元素 Qは生成発熱量 メタル分としてAlを含む滓に、酸素との親和力がAl
よりも小さい金属の酸化物を添加すると、該酸化物とA
lの間でテルミット反応が起こり、滓は加熱される。滓
中には前述の如く多量のAlがメタル分として混在して
いるので、この滓中に適量のテルミット反応性酸化物を
添加すると、該メタル分の一部との間でテルミット反応
が起こり、その激しい発熱反応によって滓は急速に加熱
される。その結果、テルミット反応に消費されなかった
残りのメタル分はこの熱により溶解して溶湯方向へ戻
り、滓層内のメタル分が低減すると共に、滓中の酸化物
はより安定で湯離れの良好な酸化物に変わり、除滓性の
優れたものになる。In the present invention, as described above, as a heating source for raising the temperature of the slag to dissolve the metal content and to change the oxide into an oxide having better removal of molten metal, an oxide (hereinafter referred to as "thermite reaction") which causes a thermite reaction with Al. , Thermite reactive oxide).
That is, the thermite reaction is, as shown by the following equation, Al
2nAl + 3MO n → nAl 2 O 3 + 3M + Q In the formula, M is an element that forms an oxide, Q is a calorific value of generation, and a slag containing Al as a metal component and oxygen. Affinity is Al
If an oxide of a smaller metal is added, the oxide and A
The thermite reaction takes place between 1 and the slag is heated. As described above, a large amount of Al is mixed as a metal component in the slag, so if a suitable amount of thermite reactive oxide is added to the slag, a thermite reaction occurs with a part of the metal component, The slag is rapidly heated by the violent exothermic reaction. As a result, the remaining metal that was not consumed in the thermite reaction was melted by this heat and returned to the direction of the molten metal, reducing the amount of metal in the slag layer, and the oxide in the slag was more stable and had good release from the molten metal. It becomes a simple oxide and has excellent slag removal properties.
【0009】この様に本発明では、滓中に多量混入して
いるメタル分(Al)を有効に活用し、テルミット反応
性酸化物との反応によって生じる急激な発熱を利用して
除滓性の向上を図るものであり、従って酸化物としては
Alとテルミット反応を生じ得るものであれば、たとえ
ばSiO2 ,Fe2 O3 ,W2 O5 ,Mo2 O5 ,Mg
O,ZrO2 の如く様々の酸化物を使用することができ
る。しかし、これらのうちFe2 O3 はテルミット反応
時の発熱量が過大で且つ急激に起こるため火災を生ずる
恐れがあり、またW2 O5 やMo2 O5 は比較的高価で
あるほか、還元により生成した元素がAl合金溶湯中に
混入すると、Al合金製品の物性に及ぼす悪影響が軽視
できないので、最も好ましいのはSiO2 もしくはこれ
に発熱量増大のため少量(2〜10重量%程度)のFe
2 O3 を混合した混合物である。As described above, in the present invention, the metal component (Al) mixed in a large amount in the slag is effectively utilized, and the rapid heat generation caused by the reaction with the thermite reactive oxide is utilized to remove the slag. As long as it is intended to improve, and therefore the oxide can cause a thermite reaction with Al, for example, SiO 2 , Fe 2 O 3 , W 2 O 5 , Mo 2 O 5 , Mg.
Various oxides such as O and ZrO 2 can be used. However, among these, Fe 2 O 3 has a possibility of causing a fire because the amount of heat generated during the thermite reaction is excessive and abruptly occurs, and W 2 O 5 and Mo 2 O 5 are relatively expensive and reduction When the element generated by the above is mixed in the molten Al alloy, the adverse effect on the physical properties of the Al alloy product cannot be neglected. Therefore, most preferable is SiO 2 or a small amount (about 2 to 10% by weight) for increasing the calorific value. Fe
It is a mixture of 2 O 3 .
【0010】ちなみにテルミット反応が起こると、前記
反応式にも示した様にAlはAl2O3 に酸化される一
方、テルミット反応性酸化物(前式におけるMOn )は
Mに還元される。この還元生成物(M)の大部分はAl
2 O3 等に吸着保持されるが、一部はAl合金溶湯中に
混入していく恐れがある。従ってテルミット反応性酸化
物としては、還元生成物としてAl合金溶湯中に混入し
難く、仮に微量混入したとしてもそれほど悪影響を及ぼ
すことのない元素の酸化物を選択するのが良い。こうし
た意味からするとSiO2 の還元生成物であるSiは、
Al合金溶湯に対する濡れ性が小さくて滓に対する濡れ
性は大きいので、溶湯に取り込まれることなく滓と共に
除去され易いという利点も有している。When the thermite reaction occurs, Al is oxidized to Al 2 O 3 as shown in the above reaction formula, while the thermite reactive oxide (MO n in the above formula) is reduced to M. Most of this reduction product (M) is Al
Although it is adsorbed and held by 2 O 3, etc., there is a risk that some of it will be mixed into the molten Al alloy. Therefore, as the thermite-reactive oxide, it is preferable to select an oxide of an element that does not easily mix as a reduction product into the molten Al alloy and does not have a bad influence even if it is mixed in a trace amount. In this sense, Si, which is a reduction product of SiO 2 , is
Since it has a low wettability with respect to the molten Al alloy and a high wettability with respect to the slag, it also has an advantage that it is easily removed together with the slag without being taken into the molten metal.
【0011】但し、溶湯内へのSiO2 やSi等の混入
を一層確実に防止するには、加熱源として添加されるテ
ルミット反応性酸化物を滓層の表層部へ添加して該表層
部のみでテルミット反応を生ぜしめ、還元生成物は滓と
共にすみやかに除去することが望まれる。However, in order to more surely prevent mixing of SiO 2 and Si into the molten metal, the thermite-reactive oxide added as a heating source is added to the surface layer of the slag layer and only the surface layer is added. Therefore, it is desired that the thermite reaction is caused and the reduction product is promptly removed together with the slag.
【0012】テルミット反応性酸化物の添加量は、生成
する滓の量に応じて変わってくるので一律に決めること
はできないが、滓層全体を十分に加熱してメタル分の溶
解と除滓性向上効果を有効に発揮させるという本発明の
趣旨を生かす意味から、滓の重量に対して0.3〜10
%、溶湯重量に対しては0.01〜0.3%程度の範囲
から選択することが望まれる。The amount of the thermite-reactive oxide added cannot be uniformly determined because it depends on the amount of slag produced, but the entire slag layer is sufficiently heated to dissolve and remove metal components. From the meaning of utilizing the gist of the present invention that the improvement effect is effectively exhibited, 0.3 to 10 relative to the weight of the slag.
%, And it is desirable to select from the range of about 0.01 to 0.3% with respect to the weight of the molten metal.
【0013】また添加されるテルミット反応性酸化物の
形態も、粉末状、粒状、破砕片状、塊状の如何を問うも
のではないが、粉塵等を生じることなく滓層の表面に均
一に散布して滓層全体を万遍なく加熱するには、粒状も
しくは破砕片状で添加するのが良い。The form of the thermite-reactive oxide added does not matter whether it is in the form of powder, granules, crushed pieces, or lumps, but it is uniformly dispersed on the surface of the slag layer without producing dust or the like. In order to uniformly heat the entire slag layer, it is preferable to add it in the form of particles or crushed pieces.
【0014】[0014]
【実施例】次に本発明の実施例を示すが、本発明はもと
より下記実施例によって制限を受けるものではなく、前
・後記の趣旨に適合し得る範囲で適当に変更して実施す
ることはいずれも本発明の技術的範囲に含まれる。EXAMPLES Examples of the present invention will be shown below. However, the present invention is not limited by the following examples, and may be appropriately modified and implemented within a range compatible with the gist of the preceding and the following. Both are included in the technical scope of the present invention.
【0015】10トン容量の重油焚き反射炉を使用し、
JIS 1100系のAl合金スクラップ(100%)
を710℃で溶解した。そして、湯面に浮上する滓に粒
状のSiO2 を溶湯重量に対して0.2%添加すると直
ちに発熱反応が起こり、滓層は5分で710℃から11
00℃に昇温した。この間、有害ガスの発生は全く認め
られなかった。次いで直ちに除滓を行なったところ、滓
の湯離れは良好で容易に除滓を行なうことができた。炉
外へ排出した滓の量は溶湯重量の約3重量%であり、且
つこの滓中に含まれるメタル分は約30重量%であり、
SiO2 を添加しないで除滓した場合の滓中のメタル含
量(80〜90重量%)に比べて大幅に減少し得ること
が確認された。尚、この除滓処理によって生じたAl合
金溶湯のSi量増加は0.01%未満であり、品質上問
題になることはなっかた。Using a heavy oil-fired reverberatory furnace with a capacity of 10 tons,
JIS 1100 series Al alloy scrap (100%)
Was melted at 710 ° C. Then, when 0.2% of granular SiO 2 was added to the slag floating on the molten metal surface with respect to the weight of the molten metal, an exothermic reaction immediately occurred, and the slag layer was heated from 710 ° C to 11 ° C in 5 minutes.
The temperature was raised to 00 ° C. During this period, no generation of harmful gas was observed. Then, when the slag was immediately removed, the slag was removed well and the slag could be easily removed. The amount of slag discharged to the outside of the furnace was about 3% by weight of the molten metal weight, and the metal content contained in this slag was about 30% by weight,
It was confirmed that the metal content in the slag (80 to 90% by weight) when the slag was removed without adding SiO 2 could be significantly reduced. The increase in the amount of Si in the molten Al alloy produced by this slag treatment was less than 0.01%, which was not a problem in terms of quality.
【0016】他方、比較例としてハロゲン系フラックス
(KCl +K2SO4 +K3AlF6+KNO3)を溶湯重量に対し0.
1%添加した以外は上記と同様にして滓の加熱と除滓を
行なったところ、上記とほぼ同程度の除滓性が得られ
た。但しこの方法では処理工程で大量の塩素ガスおよび
塩化水素ガスが発生し、作業雰囲気を著しく汚染するた
め開放状態での作業は極めて危険であり、大規模な吸引
排気ダクトを要すると共に、該排ガスを大気へ放散する
に当たっては、公害防止の観点から排ガス浄化設備の付
設が必要であった。[0016] On the other hand, the halogen-based flux (KCl + K 2 SO 4 + K 3 AlF 6 + KNO 3) molten metal relative to the weight as a comparative example 0.
When the slag was heated and the slag was removed in the same manner as above except that 1% was added, almost the same slag removal property as above was obtained. However, in this method, a large amount of chlorine gas and hydrogen chloride gas are generated in the treatment step, and the work atmosphere is significantly polluted, so work in an open state is extremely dangerous, and a large-scale suction and exhaust duct is required, and the exhaust gas is For emission to the atmosphere, it was necessary to attach exhaust gas purification equipment from the viewpoint of pollution prevention.
【0017】[0017]
【発明の効果】本発明は以上の様に構成されており、ハ
ロゲン系化合物を含まないテルミット反応性酸化物を発
熱剤として有効に活用することにより、有害ガスを生ず
ることなく滓を効率良く加熱することができ、それによ
り滓中のメタル分を効率良く溶湯へ戻すと共に滓の湯離
れ性を高めることができ、メタルロスを可及的に低減し
つつ効率良く除滓し得ることになった。EFFECTS OF THE INVENTION The present invention is constituted as described above, and by effectively utilizing thermite-reactive oxide containing no halogen compound as an exothermic agent, the slag can be efficiently heated without producing harmful gas. As a result, the metal content in the slag can be efficiently returned to the molten metal, and the slag can be removed from the molten metal efficiently, and the metal loss can be efficiently removed while the metal loss is reduced as much as possible.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 池田 隆吉 山口県下関市長府港町14番1号 株式会社 神戸製鋼所長府製造所内 (72)発明者 堂本 治 山口県下関市長府港町14番1号 株式会社 神戸製鋼所長府製造所内 (72)発明者 北野 貴之 山口県下関市長府港町14番1号 株式会社 神戸製鋼所長府製造所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takayoshi Ikeda 14-1 Chofu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Kobe Steel Works, Ltd. Chofu Works (72) Inventor Osamu Domoto 14-1 Chofu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Shares Company Kobe Steel Works Chofu Works (72) Inventor Takayuki Kitano 14-1 Chofu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Kobe Steel Works Chofu Works
Claims (2)
り、AlまたはAl合金溶湯表面の滓に、Alとテルミ
ット反応を生ずる酸化物を添加し、滓中に含まれるAl
と該酸化物との反応により滓を加熱してから除滓するこ
とを特徴とするAlまたはAl合金溶湯からの除滓法。1. When melting Al or an Al alloy, an oxide that causes a thermite reaction with Al is added to the slag on the surface of the molten Al or Al alloy, and Al contained in the slag is added.
A method for removing slag from an Al or Al alloy molten metal, characterized in that the slag is heated by a reaction of the oxide with the oxide and then removed.
鉄の混合物を使用する請求項1記載の除滓法。2. The slag removal method according to claim 1, wherein SiO 2 or a mixture thereof with iron oxide is used as the oxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8484093A JPH06299263A (en) | 1993-04-12 | 1993-04-12 | Method for removing slag from al or al alloy molten metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8484093A JPH06299263A (en) | 1993-04-12 | 1993-04-12 | Method for removing slag from al or al alloy molten metal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06299263A true JPH06299263A (en) | 1994-10-25 |
Family
ID=13841995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8484093A Withdrawn JPH06299263A (en) | 1993-04-12 | 1993-04-12 | Method for removing slag from al or al alloy molten metal |
Country Status (1)
Country | Link |
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JP (1) | JPH06299263A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6171362B1 (en) | 1998-12-25 | 2001-01-09 | Kobe Steel, Ltd | Method for refining molten aluminum alloy and flux for refining molten aluminum alloy |
WO2012161461A2 (en) * | 2011-05-20 | 2012-11-29 | 한국생산기술연구원 | Aluminium alloy and manufacturing method for same |
WO2013157903A1 (en) * | 2012-04-20 | 2013-10-24 | 한국생산기술연구원 | Aluminum alloy and method for manufacturing same |
KR101434263B1 (en) * | 2012-04-20 | 2014-08-28 | 한국생산기술연구원 | Aluminium alloy and manufacturing method thereof |
KR101434262B1 (en) * | 2012-04-20 | 2014-08-28 | 한국생산기술연구원 | Aluminium alloy and manufacturing method thereof |
-
1993
- 1993-04-12 JP JP8484093A patent/JPH06299263A/en not_active Withdrawn
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6171362B1 (en) | 1998-12-25 | 2001-01-09 | Kobe Steel, Ltd | Method for refining molten aluminum alloy and flux for refining molten aluminum alloy |
WO2012161461A2 (en) * | 2011-05-20 | 2012-11-29 | 한국생산기술연구원 | Aluminium alloy and manufacturing method for same |
WO2012161461A3 (en) * | 2011-05-20 | 2013-01-17 | 한국생산기술연구원 | Aluminium alloy and manufacturing method for same |
KR101341091B1 (en) * | 2011-05-20 | 2014-01-02 | 한국생산기술연구원 | Aluminium alloy and manufacturing method thereof |
US9657377B2 (en) | 2011-05-20 | 2017-05-23 | Korea Institute Of Industrial Technology | Aluminum alloy and production method thereof |
WO2013157903A1 (en) * | 2012-04-20 | 2013-10-24 | 한국생산기술연구원 | Aluminum alloy and method for manufacturing same |
KR101434263B1 (en) * | 2012-04-20 | 2014-08-28 | 한국생산기술연구원 | Aluminium alloy and manufacturing method thereof |
KR101434262B1 (en) * | 2012-04-20 | 2014-08-28 | 한국생산기술연구원 | Aluminium alloy and manufacturing method thereof |
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