JPH1112677A - Manufacturing method of extremely low manganese alloy - Google Patents
Manufacturing method of extremely low manganese alloyInfo
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- JPH1112677A JPH1112677A JP16645897A JP16645897A JPH1112677A JP H1112677 A JPH1112677 A JP H1112677A JP 16645897 A JP16645897 A JP 16645897A JP 16645897 A JP16645897 A JP 16645897A JP H1112677 A JPH1112677 A JP H1112677A
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Abstract
(57)【要約】
【課題】マンガン含有量が0.05重量%以下の合金
(SUS316L)を安価に製造する。
【解決手段】マンガン含有量[Mn]が0.06〜0.3
0重量%の消耗電極を用い、得るべき鋳塊の直径をD
(mm)、溶解中の真空度をP(Pa)としたとき、下記
式または式を満たす溶解速度V(kg/min )で真空ア
ーク再溶解する。
0.06≦[Mn]≦0.15の場合
0.2 ≦V≦{0.0002・D/P・([Mn]-0.05)}+2.7 ・・・・
0.15<[Mn]≦0.30の場合
0.2 ≦V≦{(0.013・D/P)+16.7}(0.3-[Mn])+0.2 ・・・・ (57) [Problem] To produce an alloy (SUS316L) having a manganese content of 0.05% by weight or less at low cost. The manganese content [Mn] is 0.06 to 0.3.
Using a 0% by weight consumable electrode, the diameter of the ingot to be obtained is D
(Mm) When the degree of vacuum during melting is defined as P (Pa), vacuum arc remelting is performed at a melting speed V (kg / min) satisfying the following expression or the expression. When 0.06 ≦ [Mn] ≦ 0.15, 0.2 ≦ V ≦ {0.0002 ・ D / P ・ ([Mn] −0.05)} + 2.7 ・ ・ ・ ・ 0.15 <[Mn] ≦ 0.30, 0.2 ≦ V ≦ {(0.013・ D / P) +16.7} (0.3- [Mn]) + 0.2 ・ ・ ・ ・
Description
【0001】[0001]
【発明の属する技術分野】本発明は、普通鋼、特殊鋼お
よびステンレス鋼に代表されるFe基合金やNi基合金
などの合金であり、合金中のマンガン含有量が0.05
重量%以下であることが要求される極低マンガン合金の
製造方法に関する。The present invention relates to alloys such as Fe-based alloys and Ni-based alloys represented by ordinary steel, special steel and stainless steel, wherein the manganese content in the alloy is 0.05.
The present invention relates to a method for producing an extremely low manganese alloy which is required to be not more than% by weight.
【0002】[0002]
【従来の技術】半導体や液晶の製造分野においては、近
年、高集積化がより一層進んでおり、例えば超LSIと
称されるデバイスの製造では、サブミクロン単位の微細
パターンの加工が必要とされている。しかし、上記のよ
うな超LSIの製造プロセスでは、微少な塵や微量の不
純物ガスが配線パターンに付着すると回路が短絡し、不
良品になる。2. Description of the Related Art In the field of manufacturing semiconductors and liquid crystals, in recent years, the degree of integration has been further increased. For example, in the manufacture of a device called a super LSI, processing of a fine pattern on a submicron unit is required. ing. However, in the above-described VLSI manufacturing process, if minute dust or a small amount of impurity gas adheres to the wiring pattern, the circuit is short-circuited, resulting in a defective product.
【0003】従って、使用される反応ガスには、高純度
で、しかもガス中に存在する微粒子(パーティクル)が
少ないものであることが要求される。このため、反応ガ
スの供給管路を構成する管材およびその付属部材には、
その内表面から放出されるパーティクルの発生が極力少
ないものであることが要求される。[0003] Therefore, the reaction gas used is required to be high in purity and low in fine particles (particles) existing in the gas. For this reason, the pipe material constituting the supply pipe of the reaction gas and its attached members include:
It is required that the generation of particles emitted from the inner surface is as small as possible.
【0004】また、半導体製造用ガスとしては、窒素、
アルゴンなどの不活性ガス以外に、塩化水素や臭化水素
などの極めて腐食性の強いガスも数多く使用される。こ
のため、上記の管材やその付属部材用の材料には、耐食
性が良好で、腐食生成物である金属化合物などのパーテ
ィクルが材料表面から発生しないものであることが要求
される。[0004] As a semiconductor manufacturing gas, nitrogen,
In addition to inert gases such as argon, many extremely corrosive gases such as hydrogen chloride and hydrogen bromide are used. For this reason, it is required that the above-mentioned tube material and the material for the attached member have good corrosion resistance and do not generate particles such as metal compounds as corrosion products from the material surface.
【0005】上記の材料としては、通常、オーステナイ
ト系ステンレス鋼が使用され、なかでも不純物元素の含
有量を規制することによって非金属介在物量を低減し、
材料表面から放出されるパーティクルの発生を減少させ
るようにしたSUS316Lが主に使用されている。As the above-mentioned material, austenitic stainless steel is usually used, and in particular, the amount of nonmetallic inclusions is reduced by regulating the content of impurity elements.
SUS316L is mainly used to reduce the generation of particles emitted from the material surface.
【0006】しかし、不純物元素のなかでもマンガン
は、蒸気圧が高いために管路製作に際しての溶接時に蒸
発し、溶接部の下流側管路内に堆積したり、パーティク
ルとして下流側に流れて汚染源となりやすい。However, among the impurity elements, manganese evaporates during welding during pipe fabrication due to its high vapor pressure, and is deposited in a pipeline downstream of a welded portion or flows as particles to the downstream side to cause contamination. It is easy to be.
【0007】従って、従来にも増してマンガン含有量を
低減できると、下記の点で極めて優れた性能を有するこ
とになる。[0007] Therefore, if the manganese content can be reduced more than ever before, it will have extremely excellent performance in the following points.
【0008】(a) 溶接時におけるマンガンヒュームの発
生が減少するために、パーティクルの発生量が少なくな
る。 (b) 管内面に対するマンガンヒュームの付着量が少なく
なるために、耐食性が向上する。 (c) 美麗な溶接ビードが得られる。 (d) 材料自体の耐食性が向上する。(A) Since the generation of manganese fume during welding is reduced, the amount of generated particles is reduced. (b) Corrosion resistance is improved because the amount of manganese fume adhering to the pipe inner surface is reduced. (c) A beautiful weld bead is obtained. (d) The corrosion resistance of the material itself is improved.
【0009】ところで、上記の管材やその付属部材の素
材となるSUS316Lに代表される合金は、従来か
ら、主として真空再溶解プロセスにより製造されてい
る。[0009] Incidentally, alloys represented by SUS316L, which are used as materials for the above-mentioned tube material and its attached members, have been conventionally produced mainly by a vacuum remelting process.
【0010】すなわち、真空誘導溶解法による一次溶解
後、消耗電極式の真空アーク再溶解法や電子ビーム溶解
法による二次溶解を行って製造されている(例えば、特
開平7−90472号公報参照)。That is, it is manufactured by performing primary melting by a vacuum induction melting method and then performing secondary melting by a consumable electrode type vacuum arc remelting method or an electron beam melting method (for example, see Japanese Patent Application Laid-Open No. 7-90472). ).
【0011】しかし、上記の真空再溶解プロセスによっ
てマンガン含有量が0.05重量%以下の合金を製造し
ようとする場合には、二次溶解の素材である消耗電極に
低マンガン材料、具体的にはマンガン含有量が少なくと
も0.06重量%未満のものを用いる必要があった。However, when an alloy having a manganese content of 0.05% by weight or less is to be produced by the above-mentioned vacuum remelting process, a low manganese material, specifically, a consumable electrode which is a material for secondary melting is used. Required that the manganese content be at least less than 0.06% by weight.
【0012】その理由は、1回の二次真空溶解で所望の
鋳塊を製造するために、得るべき鋳塊のマンガン含有量
に併せてマンガン含有量が可級的に低い消耗電極を用い
るのであるが、この場合、通常の真空アーク再溶解では
マンガンがほとんど減少しないためである。The reason is that in order to produce a desired ingot by one-time secondary vacuum melting, a consumable electrode having a manganese content that is qualitatively low in accordance with the manganese content of the ingot to be obtained is used. However, in this case, manganese hardly decreases in ordinary vacuum arc remelting.
【0013】従って、上記の一次溶解において、マンガ
ン含有量が少なくとも0.06重量%未満の低マンガン
材料を製造する必要があり、そのためには一次溶解に供
する原材料としてマンガン含有量の低い高品位な高価な
ものを用いる必要がある。また、高品位な原材料を用い
ない場合には、一次溶解時にコストのかかる特別な脱マ
ンガン処理を施す必要がある。このため、製品の製造コ
ストが著しく高くなるという問題があった。Therefore, it is necessary to produce a low manganese material having a manganese content of at least less than 0.06% by weight in the above-mentioned primary dissolution, and for that purpose, a high-grade material having a low manganese content is used as a raw material to be subjected to the primary dissolution. It is necessary to use expensive ones. If high-quality raw materials are not used, it is necessary to perform a costly special demanganese treatment at the time of the first melting. For this reason, there has been a problem that the manufacturing cost of the product is significantly increased.
【0014】なお、真空下での再溶解におけるマンガン
含有量の制御方法としては、溶解中の溶融合金からのマ
ンガン蒸発量を変化させるべく、真空度を制御する方法
がある(特公平7−081171号公報参照)。しか
し、その公報中には、マンガン含有量が0.05重量%
以下という極低マンガン合金を低コストで製造するため
の具体的方法については、一切示されていない。As a method of controlling the manganese content in remelting under vacuum, there is a method of controlling the degree of vacuum in order to change the amount of manganese evaporated from the molten alloy during melting (Japanese Patent Publication No. 7-081711). Reference). However, the publication states that the manganese content is 0.05% by weight.
No specific method for producing an extremely low manganese alloy at low cost is described below.
【0015】[0015]
【発明が解決しようとする課題】本発明は、上記の問題
点を解決するためになされたもので、その課題は、一次
溶解においてマンガン含有量の低い高品位な原材料を用
いる必要がなく、しかもコストのかかる特別な脱マンガ
ン処理を施さずとも容易に製造することが可能なマンガ
ン含有量の比較的高い電極を用いて、マンガン含有量が
0.05重量%以下の鋳塊を製造することができる極低
マンガン合金の製造方法を提供することにある。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to eliminate the need for using high-quality raw materials having a low manganese content in the primary dissolution, and It is possible to produce an ingot with a manganese content of 0.05% by weight or less using an electrode having a relatively high manganese content, which can be easily produced without performing a costly special demanganese treatment. It is an object of the present invention to provide a method for producing an extremely low manganese alloy.
【0016】[0016]
【課題を解決するための手段】本発明の要旨は、次の極
低マンガン合金の製造方法にある。The gist of the present invention resides in the following method for producing an extremely low manganese alloy.
【0017】消耗電極式真空溶解法を用いて、マンガン
含有量が0.05重量%以下の極低マンガン合金を製造
する方法であって、前記の消耗電極にマンガン含有量
[Mn]が0.06〜0.30重量%のものを用いるとと
もに、溶解炉の真空度を10Pa未満に設定したうえ
で、得るべき鋳塊の直径をD(mm)、溶解中の真空度
をP(Pa)としたとき、下記式または式を満たす
溶解速度V(kg/min)で再溶解することを特徴と
する極低マンガン合金の製造方法。A method for producing an extremely low manganese alloy having a manganese content of 0.05% by weight or less by using a consumable electrode type vacuum melting method, wherein the manganese content [Mn] of the consumable electrode is less than 0.1% by weight. In addition to using those having a melting point of 0.6 to 0.30% by weight and setting the degree of vacuum of the melting furnace to less than 10 Pa, the diameter of the ingot to be obtained is D (mm), and the degree of vacuum during melting is P (Pa). And re-melting at a dissolution rate V (kg / min) satisfying the following equation or the following equation:
【0018】0.06≦[Mn]≦0.15の場合When 0.06 ≦ [Mn] ≦ 0.15
【0019】[0019]
【数3】 (Equation 3)
【0020】0.15<[Mn]≦0.30の場合When 0.15 <[Mn] ≦ 0.30
【0021】[0021]
【数4】 (Equation 4)
【0022】上記の本発明では、マンガン含有量が0.
05重量%以下の極低マンガン合金を安価に製造する方
法として、一次真空溶解においては安価な原材料を使用
して得られる比較的高いマンガン含有量[Mn]の消耗電
極を用い、二次溶解においてマンガンの蒸発をより積極
的に行わせる方法に着目した。In the above-mentioned present invention, the manganese content is set to 0.1.
As an inexpensive method for producing extremely low manganese alloys of up to 05% by weight, in the first vacuum melting, a consumable electrode with a relatively high manganese content [Mn] obtained using inexpensive raw materials is used. We focused on a method to make manganese evaporation more active.
【0023】具体的には、真空度P、用いる消耗電極の
マンガン含有量[Mn]および得るべき鋳塊の直径Dに応
じて消耗電極の溶解速度Vを調整することによって、二
次真空溶解中の溶融合金中からのマンガン蒸発を促進さ
せてマンガン含有量が0.05重量%以下の極低マンガ
ン合金を得ることを特徴とする。Specifically, by adjusting the melting rate V of the consumable electrode according to the degree of vacuum P, the manganese content [Mn] of the consumable electrode to be used, and the diameter D of the ingot to be obtained, the secondary vacuum melting is performed. Is characterized in that manganese evaporation from the molten alloy is promoted to obtain an extremely low manganese alloy having a manganese content of 0.05% by weight or less.
【0024】[0024]
【発明の実施の形態】まず、本発明方法で得るべき合金
について説明すると、その合金はマンガン含有量が0.
05重量%以下の普通鋼、特殊鋼およびステンレス鋼に
代表されるFe基合金やNi基合金であり、マンガン以
外の成分含有量については特に規制されない。DESCRIPTION OF THE PREFERRED EMBODIMENTS First, the alloy to be obtained by the method of the present invention will be described.
It is an Fe-based alloy or Ni-based alloy typified by ordinary steel, special steel and stainless steel of not more than 05% by weight, and the content of components other than manganese is not particularly restricted.
【0025】本発明方法の重要な特徴は、一次真空溶解
において安価な原材料を使用して得られたマンガン含有
量[Mn]の比較的高い消耗電極を二次真空再溶解する
際、溶解中の真空度P(Pa)、得るべき鋳塊の直径D
(mm)および消耗電極のマンガン含有量[Mn](重量
%)に応じて消耗電極の溶解速度V(kg/min)を
調整することにより、溶融合金中からのマンガンの蒸発
を促進させて0.05重量%以下のマンガン含有量を有
する鋳塊を得ることにある。An important feature of the method of the present invention is that when a consumable electrode having a relatively high manganese content [Mn] obtained by using an inexpensive raw material in the primary vacuum melting is redissolved in the second vacuum, Degree of vacuum P (Pa), diameter D of ingot to be obtained
By adjusting the dissolution rate V (kg / min) of the consumable electrode in accordance with (mm) and the manganese content [Mn] (% by weight) of the consumable electrode, the evaporation of manganese from the molten alloy is promoted to 0. It is to obtain an ingot having a manganese content of 0.05% by weight or less.
【0026】この時、溶解炉の真空度は10Pa未満に
設定する一方、消耗電極にはマンガン含有量[Mn]が
0.06〜0.30重量%のものを用いる必要がある。
また、消耗電極の溶解速度V(kg/min)は、その
マンガン含有量[Mn]に応じて上記の式または式を
満たす速度に設定する必要がある。At this time, while the degree of vacuum of the melting furnace is set to less than 10 Pa, it is necessary to use a consumable electrode having a manganese content [Mn] of 0.06 to 0.30% by weight.
In addition, the dissolution rate V (kg / min) of the consumable electrode needs to be set to a value that satisfies the above expression or the expression according to the manganese content [Mn].
【0027】ここで、溶解炉の真空度を10Pa未満に
設定しておく必要があるのは、次の理由による。Here, it is necessary to set the degree of vacuum of the melting furnace to less than 10 Pa for the following reason.
【0028】すなわち、マンガンは、蒸気圧の高い元素
であり、真空下において蒸発しやすい。そして、その蒸
発速度は、炉内の真空度とマンガン蒸気圧の差によって
異なり、その差が小さいほど、換言すれば炉の真空度が
低いほど遅くなり、真空度が10Pa以上ではその蒸発
速度が遅くなりすぎて溶解に長時間かかり、工業的でな
くなる。また、10Pa以上の真空度では、グロー放電
が生じる危険性があり、再溶解自体が困難になる。この
ため、本発明では、溶解炉の真空度を10Pa未満に設
定することとした。That is, manganese is an element having a high vapor pressure and easily evaporates under vacuum. The evaporation rate depends on the difference between the degree of vacuum in the furnace and the manganese vapor pressure. The smaller the difference, in other words, the lower the degree of vacuum in the furnace, the slower the evaporation rate. It takes too long to dissolve because it is too slow and is not industrial. If the degree of vacuum is 10 Pa or more, there is a risk that glow discharge will occur, and it will be difficult to redissolve itself. Therefore, in the present invention, the degree of vacuum of the melting furnace is set to less than 10 Pa.
【0029】また、消耗電極にはマンガン含有量[Mn]
が0.06〜0.30重量%のものを用いる必要があ
り、その溶解速度Vは上記の式または式を満たす値
に設定する必要がある。これらは、以下に示す基礎実験
の結果による。The consumable electrode has a manganese content [Mn].
Must be 0.06 to 0.30% by weight, and the dissolution rate V must be set to the above equation or a value satisfying the above equation. These are based on the results of the basic experiments described below.
【0030】真空アーク再溶解炉(VAR炉)を用い
て、マンガン含有量[Mn](重量%)が種々異なるSU
S316L製の消耗電極を素材とし、直径Dが500m
mと800mmの鋳塊を得るに当たり、炉内の真空度P
を0.3Paと1.0Paに設定したうえで、消耗電極
の溶解速度V(kg/min)を種々変えて二次真空ア
ーク溶解を行い、得られた鋳塊のマンガン含有量を調査
した。Using a vacuum arc remelting furnace (VAR furnace), SU with various manganese contents [Mn] (% by weight) was used.
Made of S316L consumable electrode, diameter D is 500m
m and 800 mm ingot, the degree of vacuum P in the furnace
Was set to 0.3 Pa and 1.0 Pa, and a secondary vacuum arc melting was performed by variously changing the melting rate V (kg / min) of the consumable electrode, and the manganese content of the obtained ingot was investigated.
【0031】図1〜図3は、その調査結果を示し、溶解
中の炉内真空度P、得るべき鋳塊の直径D、並びに消耗
電極のマンガン含有量[Mn]と溶解速度Vとが得られた
鋳塊のマンガン含有量に及ぼす影響を示す図である。そ
して、図中には、得られた鋳塊のマンガン含有量が0.
05重量%以下であった場合を「○」印、0.05重量
%超であった場合を「▲」印で示してある。1 to 3 show the results of the investigation, in which the degree of vacuum P in the furnace during melting, the diameter D of the ingot to be obtained, the manganese content [Mn] of the consumable electrode and the melting rate V were obtained. FIG. 3 is a diagram showing the effect of a given ingot on the manganese content. And in the figure, the manganese content of the obtained ingot was 0.1%.
The case where the content was less than 05% by weight is indicated by a mark “○”, and the case where the content was more than 0.05% by weight was indicated by a mark “▲”.
【0032】図1〜図3から明らかなように、いずれの
場合も、マンガン含有量[Mn]が0.30重量%以下の
消耗電極を用い、その溶解速度Vを自身のマンガン含有
量[Mn]に応じて定まる所定の値以下にして再溶解する
と、マンガン含有量が0.05重量%以下の鋳塊が得ら
れることがわかる。As is clear from FIGS. 1 to 3, in each case, a consumable electrode having a manganese content [Mn] of 0.30% by weight or less was used, and its dissolution rate V was adjusted to its own manganese content [Mn]. It can be seen that when remelted to a predetermined value or less determined according to the above, an ingot having a manganese content of 0.05% by weight or less can be obtained.
【0033】具体的に説明すると、図1〜図3に示す結
果をまとめて溶解中の炉内真空度Pおよび得るべき鋳塊
の直径Dをも考慮し、マンガン含有量が0.05重量%
以下の鋳塊を得ることが可能な消耗電極の溶解速度Vの
上限値を式で表すと、その上限値は、消耗電極のマンガ
ン含有量[Mn]が0.06〜0.15重量%の場合、下
記式で表される値になる。また、消耗電極のマンガン
含有量[Mn]が0.15重量%超0.30重量%以下の
場合、その溶解速度Vの上限値は下記式で表される値
になる。More specifically, the results shown in FIGS. 1 to 3 are put together and the manganese content is 0.05% by weight in consideration of the degree of vacuum P in the furnace during melting and the diameter D of the ingot to be obtained.
When the upper limit of the dissolution rate V of the consumable electrode capable of obtaining the following ingot is represented by an equation, the upper limit is such that the manganese content [Mn] of the consumable electrode is 0.06 to 0.15% by weight. In this case, the value is represented by the following equation. When the manganese content [Mn] of the consumable electrode is more than 0.15% by weight and 0.30% by weight or less, the upper limit of the dissolution rate V is a value represented by the following equation.
【0034】[0034]
【数5】 (Equation 5)
【0035】[0035]
【数6】 (Equation 6)
【0036】なお、図1〜図3に示す実験結果によれ
ば、消耗電極のマンガン含有量[Mn]が0.06重量%
の場合、真空度Pの値が小さくなるにつれて、溶解速度
Vの上限は無限大に近づくが、実際には、偏析などの鋳
塊品質を考慮すると、20kg/minを超える溶解速
度Vでの溶解は避けるべきである。According to the experimental results shown in FIGS. 1 to 3, the manganese content [Mn] of the consumable electrode was 0.06% by weight.
In the case of, as the value of the degree of vacuum P decreases, the upper limit of the dissolution rate V approaches infinity. However, in actuality, when the ingot quality such as segregation is taken into consideration, the dissolution rate at a dissolution rate V exceeding 20 kg / min is considered. Should be avoided.
【0037】また、マンガンの蒸発促進には、より低い
溶解速度Vであることが望ましい。しかし、例えば、一
般的に工業的と見なされる500kg以上の鋳塊を製造
するためには、溶解速度Vを0.2kg/min未満に
したのでは42時間以上かかり、実用的でない。In order to promote the evaporation of manganese, a lower dissolution rate V is desirable. However, for example, in order to produce an ingot of 500 kg or more which is generally regarded as industrial, it takes 42 hours or more if the dissolution rate V is less than 0.2 kg / min, which is not practical.
【0038】さらに、図1〜図3に示すように、消耗電
極のマンガン含有量[Mn]が0.30重量%の場合に、
マンガン含有量が0.05重量%以下の鋳塊を得ること
が可能な消耗電極の溶解速度Vの上限値は0.2kg/
minに漸近することがわかる。Further, as shown in FIGS. 1 to 3, when the manganese content [Mn] of the consumable electrode is 0.30% by weight,
The upper limit of the dissolution rate V of the consumable electrode capable of obtaining an ingot having a manganese content of 0.05% by weight or less is 0.2 kg /
It can be seen that the value approaches to min.
【0039】一方、消耗電極のマンガン含有量[Mn]が
0.05重量%以下の場合については、再溶解時のマン
ガンピックアップがないことから、その他の条件の如何
に係わらず鋳塊のマンガン含有量は0.05重量%以下
になる。On the other hand, when the manganese content [Mn] of the consumable electrode is 0.05% by weight or less, there is no manganese pick-up at the time of re-melting. The amount will be less than 0.05% by weight.
【0040】以上のことから、本発明では、マンガン含
有量[Mn]が0.06〜0.30重量%の消耗電極を用
いるとともに、その溶解速度Vを上記の式または式
を満たす範囲内に定めることとした。From the above, according to the present invention, a consumable electrode having a manganese content [Mn] of 0.06 to 0.30% by weight is used, and the dissolution rate V is set within the above formula or a range satisfying the above formula. It was decided.
【0041】[0041]
【実施例】真空アーク再溶解炉(VAR炉)を用いて、
マンガン含有量[Mn]が種々異なる外径が130〜69
0mmのSUS316L製からなる21種類の消耗電極
を素材とし、溶解中の真空度Pと消耗電極の溶解速度V
とを種々変えて種々異なる外径Dの鋳塊を製造した。EXAMPLE Using a vacuum arc remelting furnace (VAR furnace),
Manganese content [Mn] variously different outer diameter 130-69
Using 21 types of consumable electrodes made of SUS316L of 0 mm as a material, the degree of vacuum P during melting and the dissolution rate V of the consumable electrodes
And ingots having different outer diameters D were produced.
【0042】そして、得られた鋳塊の長手方向中央部の
D/4位置から試験片を採取してマンガン含有量を調べ
た。その結果を、用いた消耗電極のマンガン含有量[M
n]、溶解中の真空度Pおよび消耗電極の溶解速度Vと
併せて表1に示した。Then, a test piece was sampled from the D / 4 position at the center in the longitudinal direction of the obtained ingot, and the manganese content was examined. Based on the results, the manganese content [M
n], the degree of vacuum P during dissolution and the dissolution rate V of the consumable electrode are shown in Table 1.
【0043】[0043]
【表1】 [Table 1]
【0044】表1に示すように、本発明の方法に従って
製造して得られた本発明例の鋳塊(No. 1〜14)は、
いずれもマンガン含有量が0.05重量%以下であっ
た。As shown in Table 1, the ingots of the present invention (Nos. 1 to 14) produced according to the method of the present invention were:
In each case, the manganese content was 0.05% by weight or less.
【0045】これに対し、消耗電極の溶解速度Vが本発
明で規定する範囲外の条件で製造して得られた比較例の
鋳塊(No. 15〜21)は、いずれもマンガン含有量が
0.06重量%以上であった。On the other hand, the ingots of the comparative examples (Nos. 15 to 21) produced under the conditions in which the dissolution rate V of the consumable electrode is out of the range specified in the present invention have a manganese content of any of them. It was 0.06% by weight or more.
【0046】[0046]
【発明の効果】本発明によれば、マンガン含有量が0.
05重量%以下の極低マンガン合金を安定して製造する
ことができる。また、素材である消耗電極にマンガン含
有量の比較的高いものを用いることができ、製造コスト
の低減が図れる。According to the present invention, the manganese content is set to 0.1.
An extremely low manganese alloy of not more than 05% by weight can be manufactured stably. In addition, a consumable electrode which is a material having a relatively high manganese content can be used, so that the manufacturing cost can be reduced.
【図1】溶解中の真空度が0.3Pa、鋳塊の直径が5
00mmの場合における消耗電極の溶解速度とマンガン
含有量とが鋳塊のマンガン含有量に及ぼす影響を示す図
である。FIG. 1 The degree of vacuum during melting is 0.3 Pa and the diameter of the ingot is 5
It is a figure which shows the influence which the dissolution rate of a consumable electrode and the manganese content have on the manganese content of an ingot in the case of 00 mm.
【図2】溶解中の真空度が1Pa、鋳塊の直径が500
mmの場合における消耗電極の溶解速度とマンガン含有
量とが鋳塊のマンガン含有量に及ぼす影響を示す図であ
る。FIG. 2 shows that the degree of vacuum during melting is 1 Pa and the diameter of the ingot is 500
It is a figure which shows the influence which the dissolution rate of a consumable electrode and manganese content have on the manganese content of an ingot in the case of mm.
【図3】溶解中の真空度が1Pa、鋳塊の直径が800
mmの場合における消耗電極の溶解速度とマンガン含有
量とが鋳塊のマンガン含有量に及ぼす影響を示す図であ
る。FIG. 3 shows that the degree of vacuum during melting is 1 Pa and the diameter of the ingot is 800
It is a figure which shows the influence which the dissolution rate of a consumable electrode and manganese content have on the manganese content of an ingot in the case of mm.
Claims (1)
含有量が0.05重量%以下の極低マンガン合金を製造
する方法であって、前記の消耗電極にマンガン含有量
[Mn]が0.06〜0.30重量%のものを用いるとと
もに、溶解炉の真空度を10Pa未満に設定したうえ
で、得るべき鋳塊の直径をD(mm)、溶解中の真空度
をP(Pa)としたとき、下記式または式を満たす
溶解速度V(kg/min)で再溶解することを特徴と
する極低マンガン合金の製造方法。 0.06≦[Mn]≦0.15の場合 【数1】 0.15<[Mn]≦0.30の場合 【数2】 1. A method for producing an extremely low manganese alloy having a manganese content of 0.05% by weight or less using a consumable electrode type vacuum melting method, wherein the consumable electrode has a manganese content [Mn]. 0.06 to 0.30% by weight, the degree of vacuum in the melting furnace is set to less than 10 Pa, the diameter of the ingot to be obtained is D (mm), and the degree of vacuum during melting is P (Pa ), Wherein the re-melting is performed at a dissolution rate V (kg / min) that satisfies the following equation or the following equation: When 0.06 ≦ [Mn] ≦ 0.15 0.15 <[Mn] ≦ 0.30
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16645897A JP4000628B2 (en) | 1997-06-24 | 1997-06-24 | Method for producing ultra-low manganese alloy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16645897A JP4000628B2 (en) | 1997-06-24 | 1997-06-24 | Method for producing ultra-low manganese alloy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1112677A true JPH1112677A (en) | 1999-01-19 |
| JP4000628B2 JP4000628B2 (en) | 2007-10-31 |
Family
ID=15831784
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16645897A Expired - Fee Related JP4000628B2 (en) | 1997-06-24 | 1997-06-24 | Method for producing ultra-low manganese alloy |
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| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008272790A (en) * | 2007-04-27 | 2008-11-13 | Sumitomo Metal Ind Ltd | Ingot manufacturing method by vacuum arc melting method |
| CN112342455A (en) * | 2020-10-28 | 2021-02-09 | 湖南华菱湘潭钢铁有限公司 | Smelting method of industrial pure iron |
-
1997
- 1997-06-24 JP JP16645897A patent/JP4000628B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008272790A (en) * | 2007-04-27 | 2008-11-13 | Sumitomo Metal Ind Ltd | Ingot manufacturing method by vacuum arc melting method |
| CN112342455A (en) * | 2020-10-28 | 2021-02-09 | 湖南华菱湘潭钢铁有限公司 | Smelting method of industrial pure iron |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4000628B2 (en) | 2007-10-31 |
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