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JPS609084B2 - Molten iron desulfurization method - Google Patents
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JPS609084B2 - Molten iron desulfurization method - Google Patents

Molten iron desulfurization method

Info

Publication number
JPS609084B2
JPS609084B2 JP10476077A JP10476077A JPS609084B2 JP S609084 B2 JPS609084 B2 JP S609084B2 JP 10476077 A JP10476077 A JP 10476077A JP 10476077 A JP10476077 A JP 10476077A JP S609084 B2 JPS609084 B2 JP S609084B2
Authority
JP
Japan
Prior art keywords
molten iron
weight
molten metal
dust
gas
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
JP10476077A
Other languages
Japanese (ja)
Other versions
JPS5438211A (en
Inventor
隆次 草川
登 川上
武司 後藤
逸雄 平野
洋一 板倉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tosoh Corp
Original Assignee
Toyo Soda Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toyo Soda Manufacturing Co Ltd filed Critical Toyo Soda Manufacturing Co Ltd
Priority to JP10476077A priority Critical patent/JPS609084B2/en
Publication of JPS5438211A publication Critical patent/JPS5438211A/en
Publication of JPS609084B2 publication Critical patent/JPS609084B2/en
Expired legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は金属溶湯の脱硫方法に関する。[Detailed description of the invention] The present invention relates to a method for desulfurizing molten metal.

金属溶湯に金属マグネシウム(以下Mg)を添加し、溶
濠中に含まれる硫黄分を除去する方法は公知である。
A method of adding magnesium metal (hereinafter referred to as Mg) to molten metal and removing sulfur contained in the molten moat is known.

しかし、Mgは蒸気圧が高く、金属(溶湯)の溶融温度
城では15気圧以上の蒸気圧を有する。
However, Mg has a high vapor pressure, and at the melting temperature of the metal (molten metal), it has a vapor pressure of 15 atmospheres or more.

従って、これを金扇溶湯に添加した際急激な反応を伴な
い、作業上極めて危険であるばかりでなく、脱硫効率も
一定せず又、Mgの反応率も低い。この様な欠点を改良
した方法として、例えば、コークスにMgを含浸させた
ものを用いる方法、鉄のターニング層の成形体にMgを
含浸させたものを用いる方法、Fe−Si−Mg合金の
ような合金を用いる方法などがあるが、これらの方法に
於いても、同伴する不純物により、金属の品位が低下し
たり、Mgの急激な反応を完全に抑制することができな
いなど、必ずしも満足すべき脱硫効果を得る方法ではな
い。本発明者らは金属溶湯の脱硫剤として用いるに適し
たMgの性状について研究を行った結果、超微粉末のM
gで「 しかもその表面が酸化マグネシウム(Mg0)
で被覆されているMgが、これを金属熔湯に添加した際
極めて効率良くかつ穏かに反応し、脱硫効率も良い事を
見出した。
Therefore, when it is added to the molten metal, it not only causes a rapid reaction, which is extremely dangerous to work with, but also the desulfurization efficiency is not constant and the reaction rate of Mg is low. Methods to improve these drawbacks include, for example, a method using coke impregnated with Mg, a method using an iron turning layer compact impregnated with Mg, and a method using a Fe-Si-Mg alloy. There are methods using alloys such as Mg, but these methods may not necessarily be satisfactory, such as the quality of the metal being degraded due to accompanying impurities or the rapid reaction of Mg not being completely suppressed. This is not a method to obtain a desulfurization effect. The present inventors conducted research on the properties of Mg suitable for use as a desulfurization agent for molten metal, and found that ultrafine powder of Mg
``Moreover, the surface is magnesium oxide (Mg0)
It has been discovered that when Mg coated with Mg is added to molten metal, it reacts very efficiently and gently, and has good desulfurization efficiency.

本発明で用いるこの様なMgを得るには、Mg0を炭素
質の還元剤で高温還元し、得られた生成物を反応系に比
較的不活性でかつ反応温度より低い温度に保ったガス、
例えばヘリウム、水素、アルゴン、窒素、或いはメタン
などの炭化水素ガス及び/又はこれらのガスに少量の一
酸化炭素ガスを含むガスと接触させて、反応温度から還
元生成物の逆反応を抑制し得る温度まで急冷して得る。
In order to obtain such Mg used in the present invention, Mg0 is reduced at high temperature with a carbonaceous reducing agent, and the resulting product is added to the reaction system with a gas that is relatively inert and kept at a temperature lower than the reaction temperature.
For example, by contacting with a hydrocarbon gas such as helium, hydrogen, argon, nitrogen, or methane and/or a gas containing a small amount of carbon monoxide gas in these gases, the reverse reaction of the reduction product can be suppressed from the reaction temperature. Obtain by quenching to temperature.

この際急冷の速度は極めて早い。この様に急冷して得た
反応生性物はMg,Mg○、炭素物質などを含むダスト
として得られる。
At this time, the speed of rapid cooling is extremely fast. The reaction products obtained by rapid cooling in this manner are obtained as dust containing Mg, Mg○, carbon substances, and the like.

このダスト中に含まれるMgは径が約10一以下概ね1
ム以下の超微粉末であり、(図一1参照)、又Mgの表
面はおおよそMg○で被覆されたものである。(図一2
参照)。得られたダストの組成は、前記した冷却ガスの
、反応生性物と接触させる際の流量、又は冷却ガス中に
含まれる一酸化炭素濃度を変えることにより任意に変え
ることができるが、通常Mg濃度として5〜95重量%
である。
The Mg contained in this dust has a diameter of approximately 10 mm or less.
It is an ultrafine powder with a size of less than 100 ml (see Figure 11), and the surface of Mg is approximately coated with Mg○. (Figure 12
reference). The composition of the obtained dust can be arbitrarily changed by changing the flow rate of the cooling gas mentioned above when it is brought into contact with the reaction product or the carbon monoxide concentration contained in the cooling gas, but usually the Mg concentration 5-95% by weight as
It is.

この組成ダストを金属落陽の脱硫剤としてそのままの形
で用いることもできるが「好ましくは、有機高分子化合
物例えばアクリル系樹脂、スチレン系樹脂、ポリビニル
アルコール、カルボキシメチルセルロースなどをそのま
ま又はベンゼン「トルェン、キシレン、酢酸エチル、メ
チルエチルケトンなど汎用の溶剤で溶解したものを用い
て成形した成形体、又は不活性雰囲気中でMgの融点以
上好ましくは1100ooまでの温度で加熱成形した成
形体として金属熔湯の脱硫に用いる事がト取扱い及び保
存の面で好ましい。前記した有機高分子物質の量は3〜
25重量%好ましくは5〜1の重量%の樹脂濃度の溶液
を前記ダストに対して5重量%以上用いることが好まし
い。
Although this composition dust can be used as it is as a desulfurizing agent for metallization, it is preferable to use an organic polymer compound such as acrylic resin, styrene resin, polyvinyl alcohol, carboxymethylcellulose, etc. as it is or to use benzene, toluene, xylene, etc. , ethyl acetate, methyl ethyl ketone, or other general-purpose solvents, or molded bodies heated and molded in an inert atmosphere at a temperature above the melting point of Mg, preferably up to 1100 oo, for desulfurization of molten metal. It is preferable to use the organic polymer substance in terms of handling and storage.
It is preferable to use a solution having a resin concentration of 25% by weight, preferably 5 to 1% by weight, based on the dust.

これら成形体の大きさは特に制限されるものではないが
、取扱いの面で0.5〜5のノ肌の球状物、ベレット状
物が好ましい。上記した方法で得たMgを含む脱硫剤を
金属溶湯に添加する方法は特に制限なく、従来の方法、
例えばキャリャーガスに脱硫剤を同伴させて吹付ける方
法、プランジャー又は鉄管に脱硫剤を充填しこれを溶湯
に浸潰して添加する方法などで行なう事ができる。窒素
ガスなどの不活性ガスをキャリヤーガスとして用いる吹
込法では、本発明の方法は添加した脱硫剤の流動性が良
い為、途中で吹込を中断する必要がなく、脱硫剤を落陽
に均一に添加できる。
The size of these molded objects is not particularly limited, but from the viewpoint of handling, spherical objects or pellet-like objects with a diameter of 0.5 to 5 mm are preferable. The method of adding the Mg-containing desulfurization agent obtained by the above method to the molten metal is not particularly limited, and conventional methods,
For example, this can be carried out by spraying the desulfurizing agent along with carrier gas, or by filling a plunger or iron pipe with the desulfurizing agent and adding it by immersing it in the molten metal. In the blowing method that uses an inert gas such as nitrogen gas as a carrier gas, the method of the present invention has good fluidity of the added desulfurizing agent, so there is no need to interrupt blowing midway through, and the desulfurizing agent can be added uniformly to the sun. can.

又従来Mgの溶湯への吹込でいまいま問題となるランス
に於ける閉塞、つまりMgの融解或いはMg3N2など
で表わされるMgの窒化物の生成による閉塞が本発明の
方法では発生しない。Mgは超微粉末では極めて自然性
に富んだものであるが、本発明はMg0などを希釈剤と
して人為的にMgの表面にそれらを被覆することなく「
元来Mg0で被覆されたMgを用いるので取扱いが極め
て安全であるばかりでなく、用いるMgが超微粉である
ので反応効率が良く従って脱硫効率が高い。
In addition, the method of the present invention does not cause blockage in the lance, which has been a problem in conventional injection of Mg into molten metal, due to melting of Mg or the formation of Mg nitrides such as Mg3N2. Mg is extremely natural in the form of ultrafine powder, but the present invention uses Mg0 as a diluent without artificially coating the surface of Mg.
Since Mg originally coated with Mg0 is used, it is not only extremely safe to handle, but also because the Mg used is an ultrafine powder, the reaction efficiency is high and the desulfurization efficiency is therefore high.

次に実施例で本発明を説明する。Next, the present invention will be explained with examples.

実施例 Mg0をオイルコークスと混合したものを原料とし「
185000で還元して得た生成物を窒素ガスと接触さ
せて急冷して得たMg含有ダストA(Mg:60重量%
、Mg0:30.5重量%、炭素:9重量%「窒素:0
.5重量%)及び冷却ガス(窒素ガス)流量を調節して
得たMg含有ダストB(Mg:30重量%、Mg0:5
3.5重量%、炭素:16重量%ト窒素三0.5重量%
)に夫々5重量%のアクリル樹脂濃度のトルェン溶液を
前記ダストに対して8重量%添加して径約0.7仇/肌
の球状とし、80℃で乾燥して得た成形体を次に述べる
ダクタィル銑鉄の脱硫試験に用いた。
Example: A mixture of Mg0 and oil coke was used as a raw material.
Mg-containing dust A (Mg: 60 wt%
, Mg0: 30.5% by weight, Carbon: 9% by weight, Nitrogen: 0
.. 5% by weight) and Mg-containing dust B (Mg: 30% by weight, Mg0:5 obtained by adjusting the flow rate of cooling gas (nitrogen gas)
3.5% by weight, carbon: 16% by weight, nitrogen 0.5% by weight
), a toluene solution with an acrylic resin concentration of 5% by weight was added to the dust in an amount of 8% by weight to form a sphere with a diameter of approximately 0.7cm/skin, and the resulting molded body was dried at 80°C. It was used in the desulfurization test of ductile pig iron described below.

銑鉄(4k9、溶湯の深さ10肌)は1400〜145
000に保ち、炭素製のランスを用いて窒素ガスをキャ
リャー(8そノ分)として前記成形体を夫々の溶湯に1
5分間吹込み、脱硫試験を行なった。
Pig iron (4k9, molten metal depth 10 skin) is 1400-145
000 and using a carbon lance as a carrier of nitrogen gas (8 parts), the molded bodies were added to each molten metal.
A desulfurization test was conducted by blowing for 5 minutes.

尚試験は大気中で行なった。又、比較の為CaC2粉(
純度80%)を前記と同様の条件で溶湯に吹込んで試験
した。
The test was conducted in the atmosphere. Also, for comparison, CaC2 powder (
(purity 80%) was blown into the molten metal under the same conditions as above.

条件及び結果を次表に示した。* 脱硫効率(%)=(
処理前の硫黄量(の‐処理後の硫黄量(の yX−−
−X IOOx 32 但しA,Bの場合x=6(M夕の量) y=24(M夕
の原子量)CaC2の場合x=16 y=64(C
aC2の分子量)尚、使用したダストAの性状は図一1
の電子顕微鏡写真(1000M音)及び電子回折像写真
で得た結果を図一2に摸式図として示した。
The conditions and results are shown in the table below. * Desulfurization efficiency (%) = (
Amount of sulfur before treatment (yX-- amount of sulfur after treatment)
-X IOOx 32 However, in the case of A and B, x = 6 (amount of M), y = 24 (atomic weight of M), in the case of CaC2, x = 16, y = 64 (C
Molecular weight of aC2) The properties of Dust A used are shown in Figure 11.
The results obtained from an electron micrograph (1000M sound) and an electron diffraction image are shown in a schematic diagram in Figure 12.

電子回析の結果から得られた格子面間隔の値は次に示す
とおりであった。
The values of lattice spacing obtained from the results of electron diffraction were as shown below.

dobs 2.80 (Spot) M夕 2.43 ′Debye) M夕02‐12
く 〃 ) 〃 1.49 ( 〃 ) 〃 dobs 1.22 ( 〃 ) 〃 1.02 (Spot) M多 又図−2中1はMg、2はMg○、3はSpoL 4は
Deのeを示す。
dobs 2.80 (Spot) M evening 2.43 'Debye) M evening 02-12
ku 〃 ) 〃 1.49 ( 〃 ) 〃 dobs 1.22 ( 〃 ) 〃 1.02 (Spot) 1 is Mg, 2 is Mg○, 3 is SpoL 4 is e of De show.

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

図一1は実施例で用いた、Mgを含むダストの電子顕微
鏡写真である。 又図一2は同じくダストの電子回折像写真で得た結果の
模式図である。図一2中1はMg、2はMg0を示す。
図一I 図一2
FIG. 11 is an electron micrograph of dust containing Mg used in Examples. Further, FIG. 12 is a schematic diagram of the results similarly obtained from an electron diffraction image photograph of dust. In FIG. 12, 1 indicates Mg and 2 indicates Mg0.
Figure 1I Figure 12

Claims (1)

【特許請求の範囲】 1 溶鉄を脱硫するに当り、超微粉金属マグネシウム及
び酸化マグネシウムを含む混合物又はその成形体を添加
することを特徴とする溶鉄の脱硫法。 2 酸化マグネシウムを高温還元して得た還元生成物を
不活性ガスと接触させて急冷し得られた金属マグネシウ
ム及び酸化マグネシウムを含む混合物を用いる特許請求
の範囲第1項記載の方法。
[Scope of Claims] 1. A method for desulfurizing molten iron, which comprises adding a mixture containing ultrafine metal magnesium and magnesium oxide, or a compact thereof, when desulfurizing molten iron. 2. The method according to claim 1, which uses a mixture containing magnesium metal and magnesium oxide obtained by contacting an inert gas with a reduction product obtained by reducing magnesium oxide at high temperature and quenching it.
JP10476077A 1977-09-02 1977-09-02 Molten iron desulfurization method Expired JPS609084B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10476077A JPS609084B2 (en) 1977-09-02 1977-09-02 Molten iron desulfurization method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10476077A JPS609084B2 (en) 1977-09-02 1977-09-02 Molten iron desulfurization method

Publications (2)

Publication Number Publication Date
JPS5438211A JPS5438211A (en) 1979-03-22
JPS609084B2 true JPS609084B2 (en) 1985-03-07

Family

ID=14389433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10476077A Expired JPS609084B2 (en) 1977-09-02 1977-09-02 Molten iron desulfurization method

Country Status (1)

Country Link
JP (1) JPS609084B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6220188A (en) * 1985-07-18 1987-01-28 Audio Technica Corp Information recording disk cleaning device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61119612A (en) * 1984-11-14 1986-06-06 Sumitomo Metal Ind Ltd Method for simultaneously removing copper and tin from molten iron

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6220188A (en) * 1985-07-18 1987-01-28 Audio Technica Corp Information recording disk cleaning device

Also Published As

Publication number Publication date
JPS5438211A (en) 1979-03-22

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