JPH07166223A - Method for recovering iron and reformed slag - Google Patents
Method for recovering iron and reformed slagInfo
- Publication number
- JPH07166223A JPH07166223A JP6300767A JP30076794A JPH07166223A JP H07166223 A JPH07166223 A JP H07166223A JP 6300767 A JP6300767 A JP 6300767A JP 30076794 A JP30076794 A JP 30076794A JP H07166223 A JPH07166223 A JP H07166223A
- Authority
- JP
- Japan
- Prior art keywords
- iron
- slag
- mixture
- raw material
- calcium fluoride
- 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.)
- Pending
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 84
- 239000002893 slag Substances 0.000 title claims abstract description 52
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims description 26
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 54
- 239000000203 mixture Substances 0.000 claims abstract description 43
- 238000009628 steelmaking Methods 0.000 claims abstract description 30
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 28
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 15
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 15
- 229910001634 calcium fluoride Inorganic materials 0.000 claims abstract description 15
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 239000011780 sodium chloride Substances 0.000 claims abstract description 10
- 239000004576 sand Substances 0.000 claims abstract description 5
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 5
- 239000012159 carrier gas Substances 0.000 claims abstract description 4
- 238000011084 recovery Methods 0.000 claims description 2
- 238000002407 reforming Methods 0.000 claims 1
- 235000013980 iron oxide Nutrition 0.000 abstract description 23
- 235000002639 sodium chloride Nutrition 0.000 abstract description 17
- 238000006243 chemical reaction Methods 0.000 abstract description 14
- 229910052782 aluminium Inorganic materials 0.000 abstract description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 8
- 229910052751 metal Inorganic materials 0.000 abstract description 5
- 239000002184 metal Substances 0.000 abstract description 5
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 abstract description 3
- SZVJSHCCFOBDDC-UHFFFAOYSA-N ferrosoferric oxide Chemical compound O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 abstract 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 1
- 239000002956 ash Substances 0.000 abstract 1
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract 1
- 229910000831 Steel Inorganic materials 0.000 description 18
- 239000010959 steel Substances 0.000 description 18
- 239000003638 chemical reducing agent Substances 0.000 description 12
- 239000003795 chemical substances by application Substances 0.000 description 10
- 238000006722 reduction reaction Methods 0.000 description 10
- 239000003832 thermite Substances 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 7
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- 238000007872 degassing Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910004261 CaF 2 Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- -1 M.Al Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000009120 camo Nutrition 0.000 description 1
- 235000005607 chanvre indien Nutrition 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000009749 continuous casting Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011487 hemp Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は製鋼原料中の酸化鉄から
鉄を回収し、かつ、改質スラグを回収する方法に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering iron from iron oxide contained in a steelmaking raw material and recovering a modified slag.
【0002】[0002]
【従来の技術】金属アルミニウム粉末と酸化鉄との混合
物は一般にテルミット剤と称され、点火するといわゆる
テルミット反応を起して高温に発熱することから発熱剤
としての用途を有し、従来からテルミット溶接法や鉄,
クロム,マンガン,コバルトなどの金属酸化物の還元冶
金法に使用されている。又、テルミット剤に使用される
金属アルミニウムに代えて、金属アルミニウムの精錬時
あるいはアルミ屑等から金属アルミニウムを再生する際
に、溶融アルミニウムの表面に生成する、いわゆるアル
ミ灰もその成分中に多量の金属アルミニウムを含有する
ことから、産業廃棄物の有効利用の一環として一部使用
されている。2. Description of the Related Art A mixture of metallic aluminum powder and iron oxide is generally called a thermite agent. When it is ignited, it causes a so-called thermite reaction to generate heat at a high temperature, and thus has a use as a heat generating agent. Law and iron,
It is used in reduction metallurgy of metal oxides such as chromium, manganese, and cobalt. Further, in place of the metal aluminum used in the thermite agent, so-called aluminum ash, which is generated on the surface of molten aluminum during refining of metal aluminum or when regenerating metal aluminum from aluminum scraps, etc. Since it contains metallic aluminum, it is partially used as part of effective utilization of industrial waste.
【0003】しかし、アーク式電気炉による製鋼法のよ
うな電気炉製鋼法にあっては、テルミット剤を添加して
その反応熱を一部利用するとしても、外部より付加すべ
き熱エネルギーは依然として大きく、又、還元力も劣る
ため製鋼に要する時間も多くかかる。そこで従来は、補
助熱源としてガス又は重油を使用して製鋼時間の短縮を
はかる必要があるなどの問題点があった。そこで本発明
者らは、かかる従来のテルミット剤を使用した電気炉製
鋼法の問題点に着目し、従来のテルミット剤に比しさら
に高い熱エネルギー及び還元力が得られる発熱還元剤を
提供するとともに、この発熱還元剤を使用した電気炉製
鋼法を発明した。However, in an electric furnace steelmaking method such as a steelmaking method using an arc type electric furnace, even if the reaction heat is partly used by adding a thermite agent, the thermal energy to be added from the outside is still present. Since it is large and the reducing power is inferior, it takes a lot of time to make steel. Therefore, conventionally, there has been a problem that it is necessary to shorten the steelmaking time by using gas or heavy oil as an auxiliary heat source. Therefore, the present inventors focused on the problems of the electric furnace steelmaking method using such a conventional thermite agent, and provide an exothermic reducing agent that can obtain higher thermal energy and reducing power than the conventional thermite agent. Invented an electric furnace steelmaking method using this exothermic reducing agent.
【0004】電気炉製鋼法に於いて用いられる製鋼原料
に酸化鉄が多く含まれる場合があるが、これら酸化鉄
は、製鋼工程の酸化期には最終的にスラグの一部となっ
て、スラグ量が増加する。ここで、このスラグから鉄を
回収することはコークス高炉で処理することにより可能
である。しかし、実際は運送や回収等の各種コストの関
係で、これら電気炉製鋼法の酸化期スラグの大部分は冷
却後破砕されて砕石として利用されているのみであり、
その価値は非常に低く、有効利用が望まれていた。The ironmaking raw materials used in the electric furnace steelmaking method may contain a large amount of iron oxide, but these iron oxides eventually become a part of the slag during the oxidation period of the steelmaking process and become slag. The amount increases. Here, it is possible to recover iron from this slag by treating with a coke blast furnace. However, in reality, due to various costs such as transportation and recovery, most of the oxidation stage slag of the electric furnace steelmaking method is only crushed after cooling and used as crushed stone,
Its value was very low, and effective utilization was desired.
【0005】[0005]
【発明が解決しようとする課題】本発明は、電気炉製鋼
法の酸化期スラグの低価値に鑑みてなされたもので、酸
化鉄を含む製鋼原料から鉄及び改質スラグを回収する方
法を提供するものである。DISCLOSURE OF THE INVENTION The present invention has been made in view of the low value of the oxidization stage slag in the electric furnace steelmaking method, and provides a method for recovering iron and reformed slag from a steelmaking raw material containing iron oxide. To do.
【0006】[0006]
【課題を解決するための手段】本発明の鉄と改質スラグ
の回収方法は、酸化鉄を含む製鋼原料に、金属アルミニ
ウム,食塩及び弗化カルシウムの混合物を添加すること
を特徴とする鉄及び改質スラグの回収方法である。本発
明の鉄と改質スラグの回収方法は、酸化鉄を含む製鋼原
料に、金属アルミニウム、食塩及び弗化カルシウムの混
合物を添加して鉄を回収した後、珪砂を添加することを
特徴とする鉄及び改質スラグの回収方法である。The method for recovering iron and modified slag according to the present invention is characterized by adding a mixture of metallic aluminum, salt and calcium fluoride to a steelmaking raw material containing iron oxide. This is a method of collecting the modified slag. The method for recovering iron and modified slag of the present invention is characterized in that a mixture of metallic aluminum, salt and calcium fluoride is added to a steelmaking raw material containing iron oxide to recover iron, and then silica sand is added. It is a method of recovering iron and modified slag.
【0007】ここで、酸化鉄を含む製鋼原料を溶融させ
て、金属アルミニウム、食塩及び弗化カルシウムの混合
物を添加する際に、キャリアガスを用いてこの混合物を
ランスから吹き込むことによって添加すれば、バブリン
グ作用により攪拌され、迅速かつ効率よく反応するので
好ましい。また、このときキャリアガスとして窒素を用
いれば、炉中に不必要な酸素が入り込まず、添加混合物
中の金属アルミニウムの還元性を有効に使えるので、好
ましい。同様に、この混合物を溶融スラグに直接添加す
ることは添加混合物の還元性の有効利用の点で好まし
い。なお、鉄を回収したのちの溶融改質スラグに珪砂を
添加することは、より改質されたスラグが得られるの
で、好ましい。以下に本発明をさらに詳細に説明する。Here, when a steelmaking raw material containing iron oxide is melted and a mixture of metallic aluminum, common salt and calcium fluoride is added, the mixture is blown from a lance with a carrier gas to add the mixture. It is preferable because it is stirred by the bubbling action and reacts quickly and efficiently. Further, at this time, it is preferable to use nitrogen as the carrier gas because unnecessary oxygen does not enter the furnace and the reducibility of metallic aluminum in the addition mixture can be effectively used. Similarly, it is preferable to add this mixture directly to the molten slag in terms of effective utilization of the reducibility of the added mixture. In addition, it is preferable to add silica sand to the melt-modified slag after recovering iron, because a more modified slag can be obtained. The present invention will be described in more detail below.
【0008】本発明で使用される金属アルミニウム(M・
Al)としては、不純物をある程度含有するものでもよ
く、前述したアルミ灰も好適に使用できる。表1にアル
ミ灰の組成の一例を示した。Metallic aluminum (M.
The Al) may contain impurities to some extent, and the aluminum ash described above can also be preferably used. Table 1 shows an example of the composition of aluminum ash.
【表1】 [Table 1]
【0009】また、酸化鉄としては、酸化物としての形
態がFe2 O3 ,Fe3 O4 ,FeOの何れであっても
よく、又、鉄鋼製品の製造時例えば連続鋳造、鋼塊、鋼
片などの圧延、鍛造等の工程で発生するいわゆるスケー
ルや、電気炉製鋼法の酸化期スラグ、或いは屑鉄も好適
に使用することができる。表2にスケールの組成の一例
を示した。The iron oxide may be any of Fe 2 O 3 , Fe 3 O 4 and FeO in the form of an oxide, and may be used in the production of steel products such as continuous casting, ingots and steel. A so-called scale generated in a process of rolling or forging a piece, a slag in the oxidation period of an electric furnace steelmaking method, or scrap iron can also be suitably used. Table 2 shows an example of the composition of the scale.
【表2】 [Table 2]
【0010】又、食塩としては原塩又は岩塩(NaCl
純度約96〜97%)の粉砕物を使用でき、さらに弗化
カルシウム(CaF2 )としては表3の組成からなる天
然の螢石の粉砕物を使用することができる。Further, as salt, raw salt or rock salt (NaCl
A pulverized product having a purity of about 96 to 97%) can be used, and as the calcium fluoride (CaF 2 ), a natural fluorite pulverized product having the composition shown in Table 3 can be used.
【表3】 [Table 3]
【0011】これらの配合組成物のうち、 M・Al,食
塩,弗化カルシウムは径1mm程度以下の細粒として使用
される。又、実施例で用いられる混合物の実用的な配合
組成とその配合割合を表4に示した。Among these blended compositions, M.Al, common salt and calcium fluoride are used as fine particles having a diameter of about 1 mm or less. Table 4 shows the practical compounding composition of the mixture used in the examples and its compounding ratio.
【表4】 本発明で用いる金属アルミニウム、食塩及び弗化カルシ
ウムの混合物は、酸化鉄を含有する製鋼原料を予め混合
して(表5参照)用いてもよい。[Table 4] The mixture of metallic aluminum, salt and calcium fluoride used in the present invention may be used by premixing a steelmaking raw material containing iron oxide (see Table 5).
【表5】 [Table 5]
【0012】参考例の発熱還元剤を使用した電気炉製鋼
法の概要について説明する。先ず図1に示すような電気
炉1(蓋及び電極は省略してある)に屑鉄3を装填する
とともに、発熱還元剤2(表5の組成のもの)を紙袋又
は麻袋に詰めて屑鉄3の堆積中間部に配置させる。これ
は発熱還元剤2は約700℃以上になると着火するため
である。次に電気炉1に蓋を覆い電極を挿入して通電す
ると、一部溶解した鋼湯は下方に流れて発熱還元剤2と
接触し、発熱還元剤2は着火して急速に反応し、激しく
発熱して高温度に上昇する。この高温によって発熱還元
剤2周辺の屑鉄3は迅速に溶解して鋼湯となり、短時間
の通電によりスケール中の酸化鉄が金属アルミニウムに
より還元されて回収され、溶鋼と一体となる。なお、従
来の電気炉製鋼法は発熱還元剤を用いない他は、この参
考例と同様にして行う。An outline of the electric furnace steelmaking method using the exothermic reducing agent of the reference example will be described. First, the scrap iron 3 is loaded into an electric furnace 1 (a lid and an electrode are omitted) as shown in FIG. 1, and the exothermic reducing agent 2 (having the composition shown in Table 5) is packed in a paper bag or a hemp bag to remove the scrap iron 3. It is placed in the middle of the stack. This is because the exothermic reducing agent 2 ignites at a temperature of about 700 ° C. or higher. Next, when the lid is covered in the electric furnace 1 and the electrode is inserted and electricity is applied, the partially melted steel hot water flows downward and comes into contact with the exothermic reducing agent 2, and the exothermic reducing agent 2 ignites and reacts rapidly and violently. Generates heat and rises to high temperature. Due to this high temperature, the scrap iron 3 around the exothermic reducing agent 2 is rapidly melted to form a steel hot water, and the iron oxide in the scale is reduced by metallic aluminum and recovered by a short-time energization, and is integrated with the molten steel. The conventional electric furnace steelmaking method is performed in the same manner as this reference example except that the exothermic reducing agent is not used.
【0013】本発明の鉄及び改質スラグの回収方法は、
図2に示すように電気炉1に装填した屑鉄3に予め通電
することにより、屑鉄の大部分が溶解して酸化期から還
元期に入る直前の溶鋼4に、ランス管5を用いて通電を
継続しながら金属アルミニウム、食塩及び弗化カルシウ
ムの混合物を吹込む。この場合、溶鋼の昇温と同時に強
力な還元、脱酸、脱リン及び脱ガス作用が行なわれ、最
終的にスラグに吸収される筈の溶鋼原料中の酸化鉄、或
いはスラグ自体に含まれる酸化鉄が還元されて鉄が回収
されて、溶鋼と一体となり、また、酸化鉄の少ない改質
スラグが回収される。また、別の効果として還元期の製
鋼時間を短縮することができる。なお、図2において6
は電気炉1の蓋、7は電極を示す。The method for recovering iron and modified slag of the present invention is
As shown in FIG. 2, by pre-energizing the scrap iron 3 loaded in the electric furnace 1, the lance pipe 5 is used to energize the molten steel 4 immediately before the oxidation period to the reduction period after most of the scrap iron is melted and enters the reduction period. While continuing, blow a mixture of aluminum metal, salt and calcium fluoride. In this case, strong reduction, deoxidation, dephosphorization, and degassing are performed simultaneously with the temperature rise of the molten steel, and the iron oxide in the molten steel raw material that should eventually be absorbed by the slag or the oxidation contained in the slag itself. The iron is reduced to recover the iron, which is integrated with the molten steel, and the modified slag containing less iron oxide is recovered. Further, as another effect, the steelmaking time in the reduction period can be shortened. In addition, in FIG.
Is a lid of the electric furnace 1, and 7 is an electrode.
【0014】[0014]
【作用】製鋼原料中の酸化鉄は金属アルミニウム、食塩
及び弗化カルシウムの混合物で還元され(還元反応の反
応式(1) 〜(3) を下に示す。)、鉄となって溶鋼と一体
になって回収されると共に、スラグ中の酸化鉄が減少
し、残部が改質スラグとなる。なお、これらの式によっ
て、金属アルミニウムのアルミニウム( Al=26.98) 1
原子に対し、酸化鉄中の鉄(Fe=55.85))1〜1.5原子
が反応して、還元されて回収されることが判る。従っ
て、スラグの量(重量)は減少する。 2Al +Fe2 O3 →2Fe +Al2 O3 +反応熱 ……(1) 2Al +3/4 Fe3 O4 →9/4 Fe +Al2 O3 +反応熱…(2) 2Al +3FeO →3Fe +Al2 O3 +反応熱 ……(3) 又、同時に金属アルミニウム、食塩及び弗化カルシウム
の混合物を吹き込むことにより脱酸、脱リン及び脱ガス
作用を促進しながらその強い還元力により還元期間を短
縮することができる。[Function] Iron oxide in the steelmaking raw material is reduced with a mixture of metallic aluminum, sodium chloride and calcium fluoride (reaction formulas (1) to (3) of the reduction reaction are shown below) to become iron and become integrated with molten steel. The iron oxide in the slag is reduced, and the rest becomes reformed slag. In addition, according to these formulas, aluminum of aluminum metal (Al = 26.98) 1
It can be seen that 1 to 1.5 atoms of iron (Fe = 55.85) in iron oxide react with the atoms and are reduced and recovered. Therefore, the amount (weight) of slag is reduced. 2Al + Fe 2 O 3 → 2Fe + Al 2 O 3 + heat of reaction …… (1) 2Al +3/4 Fe 3 O 4 → 9/4 Fe + Al 2 O 3 + heat of reaction… (2) 2Al + 3FeO → 3Fe + Al 2 O 3 + Heat of reaction (3) Simultaneously blowing in a mixture of aluminum metal, sodium chloride and calcium fluoride to accelerate deoxidation, dephosphorization and degassing, while shortening the reduction period due to its strong reducing power. You can
【0015】なお、従来の M・Alと酸化鉄との混合物
からなるテルミット剤に、食塩及び弗化カルシウムを各
少量配合した場合に、従来のテルミット剤以上の高温が
得られる理由は、上式1)〜3)に示されるような M・Al
と酸化鉄との反応により発生する熱に、式4)に示される
弗化カルシウムと食塩との高温時における置換反応によ
り発生する反応熱が加わるためと考えられる。 CaF2 +2NaCl→2NaF+CaCl2 +反応熱 ……(4) The reason why a higher temperature than the conventional thermite agent can be obtained when a small amount of each of salt and calcium fluoride is added to the conventional thermite agent composed of a mixture of M.Al and iron oxide is the above formula. M ・ Al as shown in 1) to 3)
It is considered that this is because the heat of reaction generated by the reaction between the calcium fluoride and sodium chloride shown in Formula 4) at a high temperature is added to the heat generated by the reaction between the iron oxide and iron oxide. CaF 2 + 2NaCl → 2NaF + CaCl 2 + heat of reaction …… (4)
【0016】[0016]
(参考例)容量200ton のアーク式電気炉に屑鉄18
0ton を装填し、表6の組成及び配合割合からなる混合
物1000kgを詰めた紙袋を屑鉄の中央部に配置した。
次いで蓋を覆い電極を挿入して通電(通電電圧550〜
700V)した。(Reference example) Scrap iron 18 in an electric arc furnace with a capacity of 200 tons
A paper bag filled with 0 tons and filled with 1000 kg of a mixture having the composition and the blending ratio shown in Table 6 was placed in the center of the scrap iron.
Then, cover the lid and insert the electrodes to energize (energized voltage 550 to 550
700V).
【表6】 [Table 6]
【0017】通電後一部溶解した鋼湯が下方に流れて発
熱還元剤と接触し、上記混合物は着火して一気に反応
し、この混合物周辺は約2700℃の高温に達した。こ
の温度は従来のテルミット剤による場合の約2200℃
に比し可成り高い。この高温と強い還元力により炉内の
屑鉄は迅速に溶解して酸化期及び還元期を含む溶解時間
が短縮され、出鋼までの通電時間を従来の約1時間30
分から1時間15分に短縮することができた。従って、
この短縮時間に相当する電力消費を低減することができ
た。又、溶鋼t当りの発熱還元剤の使用量は従来のテル
ミット剤の3〜4kg/tに比し1〜3kg/tと減量でき
ることが判明した。After energization, the partially melted molten steel flowed downward and contacted with the exothermic reducing agent, the mixture ignited and reacted at once, and the temperature around this mixture reached a high temperature of about 2700 ° C. This temperature is approximately 2200 ° C when using the conventional thermite agent.
Considerably higher than. Due to this high temperature and strong reducing power, the scrap iron in the furnace is quickly melted and the melting time including the oxidation period and the reduction period is shortened.
It was possible to shorten from 1 minute to 1 hour and 15 minutes. Therefore,
It was possible to reduce the power consumption corresponding to this shortened time. It was also found that the amount of the exothermic reducing agent used per molten steel t can be reduced to 1 to 3 kg / t as compared with 3 to 4 kg / t of the conventional thermite agent.
【0018】(従来の電気炉製鋼法の例)還元性混合物
を配置しない以外は参考例と同様に、容量200ton の
アーク式電気炉に屑鉄180ton を装填した。次いで蓋
を覆い電極を挿入して通電(通電電圧550〜700
V)した。酸化期から還元期に入る直前には、屑鉄に含
まれている酸化鉄、或いはカルシウムや珪素等の酸化物
が、溶鋼上に集まって溶融スラグとなっていた。この溶
融スラグは約20ton あった。その組成を調べたとこ
ろ、表7中に原料スラグとして示すとおりであった。(Example of conventional electric furnace steelmaking method) 180 tons of scrap iron was loaded into an arc type electric furnace having a capacity of 200 tons in the same manner as in the reference example except that the reducing mixture was not arranged. Then, cover the lid and insert the electrodes to energize (energizing voltage 550 to 700
V) Immediately before entering the reduction period from the oxidation period, iron oxide contained in scrap iron or oxides such as calcium and silicon gathered on molten steel to form molten slag. This molten slag was about 20 tons. When its composition was examined, it was as shown in Table 7 as a raw material slag.
【0019】(実施例1)図3に示した構造を有する滓
鍋8に、上述の電気炉溶融スラグ5ton (その組成は、
表7中に原料スラグとして示される。)を入れ、これに
前記表4の組成及び配合割合からなる混合物1200kg
をランス管10から2.5〜4kg/cm2 の窒素を用いて
5〜7分間で吹き込んだところ、スラグ温度は1350
℃付近から、1620℃まで上昇し、スラグから鉄が回
収されて鍋8の底に溶鋼が溜まった。反応後回収された
スラグの組成は表7のとおりであった。回収された還元
鉄の量は、約1200kgであった。(Embodiment 1) In a slag pan 8 having the structure shown in FIG. 3, 5 tons of the above-mentioned electric furnace molten slag (its composition is
It is shown in Table 7 as the raw material slag. ) Was added to the mixture, and 1200 kg of a mixture having the composition and blending ratio shown in Table 4 above was added.
Was blown from the lance tube 10 using nitrogen of 2.5 to 4 kg / cm 2 for 5 to 7 minutes, and the slag temperature was 1350.
The temperature rose from around 0 ° C to 1620 ° C, iron was recovered from the slag, and molten steel accumulated at the bottom of the pan 8. The composition of the slag recovered after the reaction is shown in Table 7. The amount of recovered reduced iron was about 1200 kg.
【表7】 [Table 7]
【0020】(実施例2)溶融スラグとして表8の組成
を有するものを用いたほかは実施例1と同様にして表4
の混合物の吹込を行ったところ、反応後のスラグの組成
は表8のとおりとなり、還元された溶鋼を取出口15か
ら鋳型12に注入して異型物を作ることができた。な
お、回収された還元鉄の重量は1250kgであった。Example 2 Table 4 was carried out in the same manner as in Example 1 except that the molten slag having the composition shown in Table 8 was used.
When the mixture was blown in, the composition of the slag after the reaction was as shown in Table 8, and the reduced molten steel could be injected into the mold 12 from the outlet 15 to form an atypical product. The weight of the recovered reduced iron was 1250 kg.
【表8】 [Table 8]
【0021】更に、このスラグに対して珪砂約1000
kgを窒素を用いてランスから吹き込んだところ、上記混
合物によって1620℃まで上昇していたスラグの温度
は1490℃まで低下した。こうして、ガラス化した溶
融スラグ11を鋳型12に流し出し、各種の異型物を作
ることができた。Furthermore, about 1000 g of silica sand is added to this slag.
When kg was blown from the lance with nitrogen, the temperature of the slag, which had been raised to 1620 ° C. by the above mixture, dropped to 1490 ° C. In this way, the vitrified molten slag 11 was poured into the mold 12 to make various types of atypical products.
【0022】[0022]
【発明の効果】本発明によれば、酸化鉄を含有する製鋼
原料から鉄を回収することができると同時に、改質スラ
グも回収することができる。この溶融改質スラグは、鋳
型により、各種の異型物を作成することができるもので
ある。また、上記混合物を吹き込むことにより脱酸、脱
リン及び脱ガス作用を促進しながらその強い還元力によ
り電気炉製鋼においてその還元期間を短縮することがで
きると云う副次効果も奏するものである。According to the present invention, iron can be recovered from a steelmaking raw material containing iron oxide, and at the same time, modified slag can be recovered. This melt-modified slag is capable of producing various types of atypical products by using a mold. Further, by blowing the above mixture, there is a secondary effect that the reduction period can be shortened in the electric furnace steelmaking by the strong reducing power while promoting the deoxidizing, dephosphorizing and degassing actions.
【図1】参考例の電気炉製鋼法の説明図FIG. 1 is an explanatory diagram of an electric furnace steelmaking method of a reference example.
【図2】本発明の鉄及び改質スラグの回収方法の説明図FIG. 2 is an explanatory view of a method for recovering iron and modified slag according to the present invention.
【図3】本発明の鉄及び改質スラグの回収方法の説明図FIG. 3 is an explanatory view of a method for recovering iron and modified slag according to the present invention.
【符号の説明】 1 電気炉 2 発熱還元剤 3 屑鉄 4 溶鋼 5 ランス管 6 蓋 7 電極 8 滓鍋 9 蓋 10 ランス 11 溶融スラグ 12 鋳鉄用又はスラグ用鋳型 13 スタンプ材 14 溶鋼 15 溶鋼又はスラグ取出口栓[Explanation of symbols] 1 Electric furnace 2 Exothermic reducing agent 3 Scrap iron 4 Molten steel 5 Lance tube 6 Lid 7 Electrode 8 Slag pan 9 Lid 10 Lance 11 Molten slag 12 Cast iron or slag mold 13 Stamping material 14 Molten steel or Slag removal Outlet plug
Claims (4)
ミニウム、食塩及び弗化カルシウムの混合物を添加し反
応させることを特徴とする鉄及び改質スラグの回収方
法。1. A method of recovering iron and modified slag, which comprises adding a mixture of metallic aluminum, salt and calcium fluoride to a steelmaking raw material containing iron oxide and reacting the mixture.
ミニウム、食塩及び弗化カルシウムの混合物を添加し反
応させて鉄を回収した後、珪砂を添加することを特徴と
する鉄及び改質スラグの回収方法。2. An iron and a modified slag, characterized in that a mixture of metallic aluminum, salt and calcium fluoride is added to a steelmaking raw material containing iron oxide and reacted to recover iron, and then silica sand is added. Recovery method.
ラグであることを特徴とする請求項1又は請求項2記載
の鉄及び改質スラグの回収方法。3. The method for recovering iron and modified slag according to claim 1 or 2, wherein the steelmaking raw material containing iron oxide is molten slag.
ミニウム、食塩及び弗化カルシウムの混合物をキャリア
ガスを用いて添加することを特徴とする請求項1乃至請
求項3記載の鉄及び改質スラグの回収方法。4. The iron and reforming according to claim 1, wherein a mixture of metallic aluminum, sodium chloride and calcium fluoride is added to a steelmaking raw material containing iron oxide by using a carrier gas. How to collect slag.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6300767A JPH07166223A (en) | 1994-12-05 | 1994-12-05 | Method for recovering iron and reformed slag |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6300767A JPH07166223A (en) | 1994-12-05 | 1994-12-05 | Method for recovering iron and reformed slag |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61279673A Division JPS63134622A (en) | 1986-11-26 | 1986-11-26 | Exothermic agent and electric furnace steel making method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07166223A true JPH07166223A (en) | 1995-06-27 |
Family
ID=17888852
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6300767A Pending JPH07166223A (en) | 1994-12-05 | 1994-12-05 | Method for recovering iron and reformed slag |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07166223A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2487173C1 (en) * | 2011-12-29 | 2013-07-10 | Антон Васильевич Рощин | Flux for electroslag remelting |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63134622A (en) * | 1986-11-26 | 1988-06-07 | Kazuhisa Hoshino | Exothermic agent and electric furnace steel making method |
-
1994
- 1994-12-05 JP JP6300767A patent/JPH07166223A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63134622A (en) * | 1986-11-26 | 1988-06-07 | Kazuhisa Hoshino | Exothermic agent and electric furnace steel making method |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2487173C1 (en) * | 2011-12-29 | 2013-07-10 | Антон Васильевич Рощин | Flux for electroslag remelting |
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